CN101163853B - Insulation conductor temperature-limiting heater for underground strata heating combined with three-phase y structure - Google Patents

Insulation conductor temperature-limiting heater for underground strata heating combined with three-phase y structure Download PDF

Info

Publication number
CN101163853B
CN101163853B CN200680013322.3A CN200680013322A CN101163853B CN 101163853 B CN101163853 B CN 101163853B CN 200680013322 A CN200680013322 A CN 200680013322A CN 101163853 B CN101163853 B CN 101163853B
Authority
CN
China
Prior art keywords
heater
temperature
conductor
electric conductor
heating system
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CN200680013322.3A
Other languages
Chinese (zh)
Other versions
CN101163853A (en
Inventor
C·L·桑德伯格
H·J·维讷格
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Shell Internationale Research Maatschappij BV
Original Assignee
Shell Internationale Research Maatschappij BV
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Shell Internationale Research Maatschappij BV filed Critical Shell Internationale Research Maatschappij BV
Publication of CN101163853A publication Critical patent/CN101163853A/en
Application granted granted Critical
Publication of CN101163853B publication Critical patent/CN101163853B/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • EFIXED CONSTRUCTIONS
    • E21EARTH DRILLING; MINING
    • E21BEARTH DRILLING, e.g. DEEP DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
    • E21B43/00Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
    • E21B43/30Specific pattern of wells, e.g. optimizing the spacing of wells
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L3/00Gaseous fuels; Natural gas; Synthetic natural gas obtained by processes not covered by subclass C10G, C10K; Liquefied petroleum gas
    • C10L3/06Natural gas; Synthetic natural gas obtained by processes not covered by C10G, C10K3/02 or C10K3/04
    • C10L3/08Production of synthetic natural gas
    • EFIXED CONSTRUCTIONS
    • E21EARTH DRILLING; MINING
    • E21BEARTH DRILLING, e.g. DEEP DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
    • E21B36/00Heating, cooling, insulating arrangements for boreholes or wells, e.g. for use in permafrost zones
    • E21B36/04Heating, cooling, insulating arrangements for boreholes or wells, e.g. for use in permafrost zones using electrical heaters
    • EFIXED CONSTRUCTIONS
    • E21EARTH DRILLING; MINING
    • E21BEARTH DRILLING, e.g. DEEP DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
    • E21B43/00Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
    • E21B43/16Enhanced recovery methods for obtaining hydrocarbons
    • E21B43/17Interconnecting two or more wells by fracturing or otherwise attacking the formation
    • EFIXED CONSTRUCTIONS
    • E21EARTH DRILLING; MINING
    • E21BEARTH DRILLING, e.g. DEEP DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
    • E21B43/00Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
    • E21B43/16Enhanced recovery methods for obtaining hydrocarbons
    • E21B43/24Enhanced recovery methods for obtaining hydrocarbons using heat, e.g. steam injection
    • EFIXED CONSTRUCTIONS
    • E21EARTH DRILLING; MINING
    • E21BEARTH DRILLING, e.g. DEEP DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
    • E21B43/00Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
    • E21B43/16Enhanced recovery methods for obtaining hydrocarbons
    • E21B43/24Enhanced recovery methods for obtaining hydrocarbons using heat, e.g. steam injection
    • E21B43/2401Enhanced recovery methods for obtaining hydrocarbons using heat, e.g. steam injection by means of electricity
    • HELECTRICITY
    • H05ELECTRIC TECHNIQUES NOT OTHERWISE PROVIDED FOR
    • H05BELECTRIC HEATING; ELECTRIC LIGHT SOURCES NOT OTHERWISE PROVIDED FOR; CIRCUIT ARRANGEMENTS FOR ELECTRIC LIGHT SOURCES, IN GENERAL
    • H05B2214/00Aspects relating to resistive heating, induction heating and heating using microwaves, covered by groups H05B3/00, H05B6/00
    • H05B2214/03Heating of hydrocarbons

Abstract

A heating system for a subsurface formation is described. The heating system includes a first heater (212), a second heater (212), and a third heater (212) placed in an opening in the subsurface formation. Each heater includes an electrical conductor (218), an insulation layer (220) at least partially surrounding the electrical conductor, and an electrically conductive sheath (222) at least partially surrounding the insulation layer. The electrical conductor is electrically coupled to the sheath at a lower end portion of the heater. The lower end portion is the portion of the heater distal from a surface of the opening. The first heater, the second heater, and the third heater are electrically coupled at the lower end portions of the heaters. The first heater, the second heater, and the third heater are electrically coupled in a three-phase wye configuration.

Description

The insulation conductor temperature-limiting heater that is used for the subterranean strata heating with the three-phase y structure combination
Technical field
Present invention relates in general to be used for method and system by various subterranean stratas (such as the rock stratum of hydrocarbonaceous) heating and production hydrocarbon, hydrogen and/or other products.Embodiment relates to the insulation conductor temperature-limiting heater that is used for heating subterranean strata.
Background technology
The hydrocarbon that is obtained by subterranean strata is used as the energy, raw material and consumer products usually.The consideration that exhausts for available hydrocarbon source and made that for the consideration that the total amount of production hydrocarbon reduces having developed a lot of technologies obtains the more effective recovery in available hydrocarbon source, processing and/or use.On-the-spot technology can be used to hydrocarbon feed is removed from subterranean strata.The chemistry of hydrocarbon feed and/or physical property possibly need to change to allow hydrocarbon feed can be easier to from subterranean strata, remove in the subterranean strata.Chemistry and physical change can comprise the real-world effectiveness of the removable fluid, composition variation, solubility variation, variable density, phase change and/or the viscosity variation that produce hydrocarbon feed in the rock stratum.Fluid can be the solid particle flows that gas, liquid, suspension, mud and/or flowing property are similar to flow, but is not limited to this.
Heater can place pit shaft with technology heats rock stratum at the scene.The example of on-the-spot technology that utilizes donwhole heater at the United States Patent(USP) No. of authorizing Ljungstrom 2,634,961, authorize the United States Patent(USP) No. 2,732 of Ljungstrom; 195, authorize Ljungstrom United States Patent(USP) No. 2,780,450, authorize the United States Patent(USP) No. 2 of Ljungstrom; 789,805, authorize the United States Patent(USP) No. 2,923 of Ljungstrom; 535, authorize shown in the United States Patent(USP) No. 4,886,118 of Van Meurs etc.; All these patents equally are incorporated into this through reference as describing fully here.
Heat is put on oil shale layer to be described in the United States Patent(USP) No. of authorizing Ljungstrom 2,923,535 and the United States Patent(USP) No. 4,886,118 of authorizing Van Meurs etc.Heat can put on oil shale layer with the oil bearing rock in the pyrolysis oil rammell.Heat also can make rock breakdown to increase the permeability of rock stratum.The permeable performance that increases allows formation fluid to march to the producing well that fluid is removed from oil shale layer.In the more disclosed technologies of Ljungstrom, for example, oxygen containing gaseous medium is introduced permeable rock stratum, the heat from preheating step is preferably still arranged simultaneously, to start burning.
Thermal source can be used to heat subterranean strata.Electric heater can be used to heat subterranean strata through radiation and/or conduction.Element of electric heater adjustable resistance ground heating.Authorize the United States Patent(USP) No. 2,548,360 of Germain and described a kind of electrical heating elements that places the viscous oil in the pit shaft, this patent equally is incorporated into this through reference as describing fully here.The heater element heats oil also makes it thinning to allow oil pumping from pit shaft.The United States Patent(USP) No. 4,716,960 of authorizing Eastlund etc. has been described through letting the electric current of relative low-voltage pass pipeline that pipeline comes the electric oil well preventing to form solid, and this patent is through with reference to equally being incorporated into this as describing fully here.Authorize the United States Patent(USP) No. 5,065,818 of Van Egmond and described a kind of electrical heating elements that is bonded in the pit shaft and does not have sleeve to surround, this patent equally is incorporated into this through reference as describing fully here.
Some heaters possibly be difficult to be combined in the subterranean strata.Electric current between the donwhole heater in the subterranean strata may be owing to the unstability that is difficult to form electric current in underground connection and the underground situation and is unreliable.Thereby, advantageously having a kind of heater, it is the electric current between underground heater not.
Summary of the invention
Embodiment described here relates generally to system, method and the heater that is used to handle subterranean strata.Embodiment described here also relates to the heater that wherein has novel components generally.This heater can obtain through using system and method described here.
In certain embodiments, the invention provides one or more systems, method and/or heater.In certain embodiments, these systems, method and/or heater are used to handle subterranean strata.
In certain embodiments, a kind of heating system that is used for subterranean strata, it comprises: be arranged in primary heater, secondary heater and the 3rd heater in the opening in the subterranean strata, wherein each heater comprises: electric conductor; Surround the electrical insulator of electric conductor at least in part; Surround the conductive jacket of electrical insulator at least in part; Wherein electric conductor is bonded to sheath at the end portion electricity of heater, and said end portion is the heater section of heater away from open surfaces; Primary heater, secondary heater and the 3rd heater combine at the end portion electricity of heater; With primary heater, secondary heater and the 3rd heater configuration is to combine with the three-phase y structure electricity.
According to another aspect of the present invention, a kind of heating system that is used for subterranean strata is provided, has comprised:
Be arranged in primary heater, secondary heater and the 3rd heater in the opening in the subterranean strata, wherein each heater comprises:
Electric conductor;
Surround the electrical insulator of electric conductor at least in part;
Surround the conductive jacket of electrical insulator at least in part;
Wherein electric conductor is bonded to sheath at the end portion electricity of heater, and said end portion is the part away from open surfaces of heater;
Primary heater, secondary heater and the 3rd heater combine at the end portion electricity of heater; With
Primary heater, secondary heater and the 3rd heater configuration are to combine with the three-phase y structure electricity;
Wherein this system also comprises support component, and primary heater, secondary heater and the 3rd heater are bonded to this support component;
Wherein electric conductor comprises:
The internal layer electric conductor;
Surround internal layer electric conductor and the electric ferromagnetic conductor that is bonded to the internal layer electric conductor at least in part;
Electricity is bonded to the outer electric conductor of ferromagnetic conductor, and this skin electric conductor surrounds ferromagnetic conductor at least in part, and outer electric conductor is lower than most of resistive thermal output that heater is provided under the about 50 ℃ temperature of selected temperature reaching; With
One or more electrical insulators that surround outer electric conductor at least in part.
According to another aspect of the present invention, a kind of method that is used for installing at subterranean strata said heating system is provided, this method comprises:
The position of the opening in subterranean strata is positioned at primary heater on first bobbin, secondary heater is positioned on second bobbin and with the 3rd heater be positioned on the 3rd bobbin;
In the time of in the said opening that heater is installed in the subterranean strata, with each unwinding of primary heater, secondary heater and the 3rd heater;
In the time of in the said opening that heater is installed in the subterranean strata, in conjunction with each heater; With
With three-phase y structure electricity heater-combining.
According to another aspect of the present invention, a kind of method of utilizing said heating system to heat is provided, this method comprises the heat from heater is offered a part of subterranean strata.
In a further embodiment, can be combined from the characteristics of specific embodiment with characteristics from other embodiment.For example, can be combined from the characteristics of an embodiment with characteristics from any other embodiment.
In a further embodiment, utilize any method, system or heater described here to carry out the processing of subterranean strata.
In a further embodiment, extra characteristics can increase to specific embodiment described here.
Description of drawings
Under below benefiting from, describing in detail and with reference to accompanying drawing, advantage of the present invention will become obviously for those skilled in the art, in the accompanying drawings:
Fig. 1 shows the stage of heating hydrocarbon-containing formation.
Fig. 2 shows the sketch map of embodiment of the part of the on-the-spot conversion system that is used to handle hydrocarbon-containing formation.
Fig. 3 A and 3B show the cross-sectional view of the embodiment of the temperature-limiting heater parts that are used for insulated conductor heater.
Fig. 4 A and 4B show the embodiment that is used for installing at pit shaft heater.
Fig. 4 C shows the embodiment that sheath is shorted to the insulated electric conductor of conductor.
Fig. 5 A and 5B show the embodiment of the heater that has three conductors in the pipeline.
Though the present invention can be easy to carry out various modifications and alternative forms, its specific embodiment illustrates and will describe in detail here by means of the example in the accompanying drawing.Accompanying drawing possibly not be pro rata.Yet be to be understood that its accompanying drawing is not limited to disclosed concrete form with the present invention with describing in detail, but opposite, the present invention should cover and fall into the present invention and like the interior all modifications of spirit that claim limits and scope enclosed, be equal to and replace.
The specific embodiment
Following description relates generally to the system and method that is used for handling the rock stratum hydrocarbon.This rock stratum can be processed to produce hydrocarbon product, hydrogen and other products.
" hydrocarbon " is normally defined the molecule that mainly is made up of carbon and hydrogen atom.Hydrocarbon also can comprise other element, is such as but not limited to halogen, metallic element, nitrogen, oxygen and/or sulphur.Hydrocarbon can be kerogen, pitch, pyrobitumen, oil, natural mineral wax and natural rock asphalt, but is not limited thereto.Hydrocarbon can be arranged near earth mineral matrices or its.Matrix can include but not limited to: sedimentary rock, sand, silicilyte, carbonate, kieselguhr and other porous media." hydrocarbon fluid " is the fluid that comprises hydrocarbon.Hydrocarbon fluid can comprise, carries or be carried in the non-hydrocarbon fluids, such as hydrogen, nitrogen, carbon monoxide, carbon dioxide, hydrogen sulfide, water and ammonia.
" rock stratum " comprises layer, cap rock and/or the underlying stratum of the layer of one or more hydrocarbonaceous, one or more no hydrocarbon." cap rock " and/or " underlying stratum " comprises one or more dissimilar impermeable materials.For example, cap rock and/or underlying stratum can comprise the carbonate of rock, shale, mud stone or wet/closely.At the scene among some embodiment of converting process; Cap rock and/or underlying stratum can comprise and can not stand the hydrocarbon bearing formation of temperature at the scene during the converting process that this temperature can cause the tangible change of properties of the hydrocarbon bearing formation of cap rock and/or underlying stratum impermeable relatively.For example, the underlying stratum can comprise shale or mud stone, but the underlying stratum can not be heated to pyrolysis temperature during the converting process at the scene.In some cases, cap rock and/or underlying stratum can be permeable a little.
" thermal source " is any system that is used for through conduction and/or transfer of radiant heat heat being offered basically at least a portion rock stratum.For example, a kind of thermal source can comprise and places ducted electric heater, such as insulated electric conductor, elongated member and/or conductor.A kind of thermal source also can comprise the system that produces heat through combustion fuel in rock stratum outside or wherein.This system can be surface burners, downhole gas burner, flameless distributed combustor and natural distributed combustor.In certain embodiments, offer one or more thermals source or the heat that in said thermal source, produces can be supplied by other energy.Other energy is heated formation directly, and perhaps energy can be supplied to the transmission medium of direct or indirect heated formation.It is to be understood that the one or more thermals source that heat put on the rock stratum can use the different energy.Thereby; For example; For given rock stratum; Some thermals source can be supplied the heat from resistance heater, and some thermals source can provide the heat of spontaneous combustion, and some thermals source can provide the heat from one or more other energy (for example chemical reaction, solar energy, wind energy, biomass or other renewable energy resource).Chemical reaction can comprise exothermic reaction (for example, oxidation reaction).Thermal source also can comprise heat is offered near the heating location and/or surrounds the heater in the zone of this heating location (such as heater well).
" heater " is to be used for producing hot any system or thermal source at well or pit shaft near zone.Heater can be electric heater, burner, with the material in the rock stratum or the burner and/or its combination that react by the material that the rock stratum produced.
" on-the-spot converting process " refers to be increased to the temperature with at least a portion rock stratum by thermal source heating hydrocarbon-containing formation and is higher than pyrolysis temperature so that in the rock stratum, produce the technology of pyrolyzation fluid.
" insulated electric conductor " refers to can conduct electrical power and on the whole or any elongated material that is partly covered by electrically insulating material.
Elongated member can be metal heater that exposes or the metal heater that exposes." exposed metal " and " metal of exposure " refer to the metal that does not comprise electric insulation layer (such as mineral insulation, its design provides electric insulation to metal in the operating temperature range of elongated member).The exposed metal and the metal of exposure can be contained the metal that comprises corrosion inhibitor, such as the oxide layer of Lock-in, the oxide layer that applies and/or film.The exposed metal and the metal of exposure comprise the metal that has polymer or under the typical operation temperature of elongated member, can not keep other type of electrical insulation of electrical insulation property.This material can be arranged on the metal and can thermal degradation between the operating period of heater.
" temperature-limiting heater " is commonly referred to as the heater of regulating the thermal output (for example reducing thermal output) that is higher than specified temp under the peripheral control unit (such as temperature controller, electric energy regulator, rectifier or miscellaneous equipment) not using.Temperature-limiting heater can be the resistance heater that AC (interchange) or modulation (for example " slicing ") DC (direct current) drive.
" Curie temperature " is one and is higher than the temperature that this temperature ferrimagnet just loses its all ferromagnetic properties.Except when being higher than Curie temperature, losing its all ferromagnetic properties, ferromagnetic material just begins to lose its ferromagnetic property when the electric current that increases passes ferrimagnet.
" time variable-current " refers to and in ferromagnetic conductor, produces kelvin effect electric current and amplitude time-varying current.The time variable-current comprises interchange (AC) and modulation direct current (DC).
" exchange (AC) " and refer to the time variable-current of sinusoidal ground reverses direction basically.AC produces the kelvin effect electric current in ferromagnetic conductor.
" modulation direct current (DC) " refers to any non-sinusoidal basically time variable-current that in ferromagnetic conductor, produces the kelvin effect electric current.
" regulate than " of temperature-limiting heater is the ratio between the most low-resistance on the highest AC or modulation DC resistance and the Curie temperature under the Curie temperature for given electric current.
With regard to the heating system that reduces thermal output, apparatus and method; Term " automatically " means and is not using peripheral control unit (for example; Peripheral control unit; Such as controller, PID controller or predictive controller with temperature pick up and backfeed loop) under with the acting this system of certain mode, apparatus and method.
Term " pit shaft " refers to through boring or with pipeline and inserts the rock stratum and the hole that in the rock stratum, forms.Pit shaft can have the circular cross section, perhaps another shape of cross section.As used herein, can exchange ground with word " pit shaft " during opening in relating to the rock stratum of word " well " and " opening " and use.
Hydrocarbon in the rock stratum can be handled to produce a lot of Different products in every way.In certain embodiments, the hydrocarbon in the rock stratum is handled by stages.Fig. 1 shows the stage of heating hydrocarbon-containing formation.Fig. 1 also shows from the formation fluid of the rock stratum example with the productivity ratio (" Y ", unit are bucket) (y axle) of oil equivalent per ton and the temperature of heated formation (" T ", unit are degree centigrade) (x axle).
The desorb of methane and evaporation of water took place between period of heating phase I.Can carry out as soon as possible through the phase I heated formation.For example, when hydrocarbon-containing formation during by initial heating, the hydrocarbon in the rock stratum is separated the methane that sucking-off absorbs.The methane of desorb can produce from the rock stratum.If hydrocarbon-containing formation further is heated, the water evaporation in the hydrocarbon-containing formation.In some hydrocarbon-containing formations, water may take the void content of rock stratum 10% to 50%.In other rock stratum, water takies greater or lesser void content.Water is usually between 160 ℃ to 285 ℃, evaporate from the rock stratum under the absolute pressure of 600kPa to 7000kPa.In certain embodiments, the rock pressure of variation of the wettable in the water generates rock stratum of evaporation and/or increase.Wettable changes and/or increased pressure can influence pyrolytic reaction or other reaction in the rock stratum.In certain embodiments, the water of evaporation produces from the rock stratum.In other embodiments, the water of evaporation is used for drawing gas and/or distill outside rock stratum or the rock stratum.Water is removed from the rock stratum and increased the memory space that void content in the rock stratum can increase hydrocarbon in the void content.
In certain embodiments, after the phase I heating, the rock stratum is further heated, so that the temperature in the rock stratum (at least) reaches beginning pyrolysis temperature (such as the lower end that is in temperature range shown in second stage).Hydrocarbon in the rock stratum can pyrolysis in second stage.Pyrolysis temperature range changes according to the type of hydrocarbon in the rock stratum.Pyrolysis temperature range can comprise the temperature between 250 ℃ to 900 ℃.Be used to produce the extensible only part of crossing the total pyro lysis temperature temperature range of pyrolysis temperature range of expected product.In certain embodiments, the pyrolysis temperature range that is used to produce expected product comprises the temperature between temperature or 270 ℃ to 350 ℃ between 250 ℃ to 400 ℃.If the temperature of hydrocarbon 250 ℃ to 400 ℃ the temperature range of associating that raises lentamente in the rock stratum, the production of pyrolysis product is accomplished during near 400 ℃ in temperature basically.The average temperature of hydrocarbon can with less than 5 ℃/day, less than 2 ℃/day, less than 1 ℃/day or raise in order to the pyrolysis temperature range of production expected product less than 0.5 ℃/day speed.Rock stratum with a plurality of thermals source heating hydrocarbonaceous can form thermal gradient around thermal source, this temperature with hydrocarbon in rock stratum pyrolysis temperature range that raise lentamente.
For the product of expectation, the raise speed of pyrolysis temperature range of temperature may be influenced the quality and the quantity of the formation fluid that is produced by hydrocarbon-containing formation.For the product of expectation, the temperature pyrolysis temperature range that raise lentamente may be suppressed moving of long-chain molecule in the rock stratum.For the product of expectation, the temperature pyrolysis temperature range that raise lentamente may be limited generation and do not hope the reaction between the mobile hydrocarbon of product.For the product of expectation, the rock temperature pyrolysis temperature range that raise lentamente may be allowed the hydrocarbon by formation production high-quality, high API severe.Product for expectation may allow the rock temperature pyrolysis temperature range that raise lentamente a large amount of hydrocarbon that occur in the rock stratum are removed as hydrocarbon product.
In some on-the-spot embodiment that change, replace lentamente temperature being heated a temperature range, a part of rock stratum is heated to desired temperatures.In certain embodiments, preferred temperature is 300 ℃, 325 ℃ or 350 ℃.Other temperature also may be selected to be preferred temperature.Stack from the heat of thermal source allows in the rock stratum, to form relatively fast and effectively preferred temperature.Scalable is in preferred temperature from the energy input of thermal source to rock stratum with the temperature of keeping the rock stratum basically.The part that is heated of rock stratum maintains preferred temperature basically and descends so that become uneconomical by formation production expectation formation fluid up to pyrolysis.The rock stratum part that receives pyrolysis can comprise the zone of only being gone into pyrolysis temperature range from the torrid zone of a thermal source transmission.
In certain embodiments, the formation fluid that comprises pyrolyzation fluid is from formation production.Along with the temperature increase of rock stratum, the amount of condensable hydrocarbon can reduce in the formation fluid of generation.At high temperature, the rock stratum produces methane and/or hydrogen mostly.If hydrocarbon-containing formation was heated whole pyrolysis range, the rock stratum can only produce the little hydrogen towards the pyrolysis range upper limit.After all available hydrogen exhaust, the minimum fluid production in rock stratum will take place usually.
After the hydrocarbon pyrolysis, a large amount of carbon maybe be still in the rock stratum with some hydrogen.The a large amount of carbon that remain in the rock stratum can be produced by the form of rock stratum with synthesis gas.Synthesis gas produces and can between period of heating phase III shown in Figure 1, take place.Phase III can comprise hydrocarbon-containing formation is heated to the temperature that is enough to allow synthesis gas to produce.For example, synthesis gas can produce to about 1000 ℃ temperature range from about 400 ℃ to about 1200 ℃, about 500 ℃ to about 1100 ℃ or about 550 ℃.The rock stratum is heated the component of the synthesis gas that the temperature of part when synthesis gas produces fluid and is introduced into the rock stratum determined to produce in the rock stratum.The synthesis gas that produces can be removed from the rock stratum through producing well.
The total interior of producing from hydrocarbon-containing formation of fluid can keep constant relatively pyrolysis and synthesis gas manufacturing process.During pyrolysis under the low relatively rock temperature, the considerable part of the fluid that produces possibly be the condensable hydrocarbon with high interior ability.Yet under higher pyrolysis temperature, less formation fluid possibly comprise the condensable hydrocarbon.More incoagulable formation fluid can be produced from the rock stratum.Can, overriding not condensable formation fluid may reduce a little during producing in the per unit volume of the fluid that produces.During synthesis gas produces, can compare remarkable reduction with the interior of pyrolyzation fluid in the per unit volume of the synthesis gas that produces.Yet the volume of the synthesis gas that produces will enlarge markedly under many circumstances, thus the interior ability that compensation reduces.
Fig. 2 shows the sketch map of an embodiment of the part of the on-the-spot conversion system that is used to handle hydrocarbon-containing formation.On-the-spot conversion system can comprise barrier wells (barrier well) 200.Barrier wells 200 is used for around processing region, forming the barrier layer.The anti-fluid in barrier layer flows into and/or the outflow processing region.Barrier wells include but not limited to anhydrate well, negative pressure well, catch well, injector well, mortar well, freeze well or its combination.In the embodiment shown in Figure 2, barrier wells 200 only is depicted as along a side of thermal source 202 extends, but barrier wells is used for maybe will being used for the thermal source 202 of heated formation processing region around all usually.
Thermal source 202 is arranged at least a portion rock stratum.Thermal source 202 can comprise heater, such as conductor heater, surface burners, flameless distributed combustor and/or natural distributed combustor in insulated electric conductor, the pipeline.Thermal source 202 also can comprise the heater of other type.Thermal source 202 offers at least a portion rock stratum with the hydrocarbon in the heated formation with heat.Energy can be supplied to thermal source 202 through supply line 204.Supply line 204 can be according to being used for the type of thermal source of heated formation and structurally different.The supply line 204 that is used for thermal source can be electric heater and transmits electric energy, can be the burner transfer the fuel, perhaps can carry the heat-exchange fluid that circulates in the rock stratum.
Producing well 206 is used for formation fluid is removed from the rock stratum.In certain embodiments, producing well 206 can comprise one or more thermals source.Thermal source in the producing well can heat one or more parts of producing well place or near the rock stratum of producing well.The condensing and reflux of the formation fluid that thermal source in the producing well can suppress from the rock stratum, to remove.
The formation fluid of being produced by producing well 206 can be delivered to treatment facility 210 through conduit 208.Formation fluid also can be produced by thermal source 202.For example, fluid can be produced with the pressure near the rock stratum control thermal source by thermal source 202.The fluid of being produced by thermal source 202 can be delivered to conduit 208 or the fluid produced can directly be delivered to treatment facility 210 through pipeline or pipeline through pipeline or pipeline.Treatment facility 210 can comprise separative element, reaction member, upgrading unit, fuel cell, turbine, storage container and/or other system and the unit that are used for the formation fluid that is produced is handled.
Temperature-limiting heater can be by under some temperature, the material structure of automatic temperature-adjusting restriction character being provided and/or comprising said material for heater.In certain embodiments, ferrimagnet is used for temperature-limiting heater.When the time, variable-current was applied to ferrimagnet, ferrimagnet can the Curie temperature place of material or near from limit temperature, so that the heat of Curie temperature place or near reduction to be provided.In certain embodiments, ferrimagnet can limit the temperature of temperature-limiting heater certainly at the selected temperature place of asymptotic Curie temperature.In certain embodiments, selected temperature be in about 35 ℃ of Curie temperature, in about 25 ℃, in about 20 ℃ or in about 10 ℃.In certain embodiments, ferrimagnet and other material (for example, high conductance material, high-strength material, resistant material or its combination) combine so that different electric and/or engineering properties to be provided.The some parts of temperature-limiting heater can have the resistance that other part of proportional limit temperature heater will be low (because different geometries and/or owing to use different ferromagnetism and/or nonferromugnetic material to cause).Make the each several part of temperature-limiting heater have different materials and/or size allows the thermal output by each partial design expectation of heater.
Temperature-limiting heater is more reliable than other heater.Temperature-limiting heater is not easy to destroy or be out of order owing to the focus in the rock stratum.In certain embodiments, temperature-limiting heater allows rock stratum heating as one man basically.In certain embodiments, temperature-limiting heater can through along whole length of heater with higher evenly heat output function heated formation more effectively.Temperature-limiting heater along whole length of heater with higher evenly heat output function, if because the power that surpasses or will surpass the maximum operating temp heater of heater along the temperature of any point of heater need not to be reduced to whole heater as typical constant watt heater that kind.Under the situation of the controlled adjustment of the time variable-current that is not applied to heater, automatically reduce from the heat near the part output of heater Curie temperature of temperature-limiting heater.Thermal output automatically reduces owing to the variation of electrical property (for example resistance) aspect of the part of temperature-limiting heater.Thereby, during more most heating process, the more power of temperature-limiting heater supply.
In certain embodiments, the system that comprises temperature-limiting heater provide at first first thermal output and then when electric current that temperature-limiting heater was changed by the time encourages near the Curie temperature of the active component of heater, the thermal output (second thermal output) of reduction is provided on Curie temperature place or the Curie temperature.First thermal output is the thermal output when following temperature, promptly is lower than this temperature temperature-limiting heater and begins from restriction.In certain embodiments, first thermal output is that temperature is 50 ℃, 75 ℃, 100 ℃ or 125 ℃ of thermal outputs of locating under the Curie temperature of ferrimagnet in the temperature-limiting heater.
Temperature-limiting heater can be encouraged by the time variable-current (exchanging or the modulation direct current) in the supply of well head place.Well head can comprise power source and be used for other parts (for example modulating part, transformer and/or capacitor) with power supply to temperature-limiting heater.Temperature-limiting heater can be to be used for one of a lot of heaters that heat a part of rock stratum.
When in certain embodiments, the temperature-limiting heater electric current that is included in free variation applies on it as the conductor of kelvin effect or kindred effect heater.Kelvin effect has limited electric current and has penetrated the inner degree of depth of conductor.For ferrimagnet, kelvin effect is by the permeability domination of conductor.The relative permeability of ferrimagnet usually between 10 and 1000 (for example, the relative permeability of ferrimagnet be at least usually 10 and can be at least 50,100,500,1000 or bigger).Be higher than Curie temperature and/or work as the electric current that is applied when increasing when the temperature of ferrimagnet is increased to, the permeability of ferrimagnet significantly reduces and the depth of penetration is expanded (for example, the depth of penetration expand to permeability inverse square root) rapidly.The reduction of permeability cause the Curie temperature place, neighbouring or on and/or when the electric current that applies increases the AC or the modulation DC resistance of conductor reduce.When temperature-limiting heater is encouraged by the power supply of substantial constant, approaching, reach or the heater section that is higher than Curie temperature can have the dissipation of heat of reduction.Temperature-limiting heater be not near Curie temperature or its part can be by the dissipation of heat that allows heater because higher ohmic load and very high kelvin effect heating is arranged.
Use temperature-limiting heater to come the advantage of the hydrocarbon in the heated formation to be, conductor is selected as has the Curie temperature that is in the desired operation temperature range.Operation in the desired operation temperature range allows significant thermojet to go into the rock stratum to keep the temperature of temperature-limiting heater and miscellaneous equipment simultaneously and be lower than the design limitations temperature.The design limitations temperature is the temperature that the character such as burn into creep and/or distortion and so on affects adversely.The temperature limitation character of temperature-limiting heater has prevented near heater overheated low heat conductivity " focus " of rock stratum or has burnt.In certain embodiments; Temperature-limiting heater can reduce or control thermal output and/or hold out against temperature and is higher than 25 ℃, 37 ℃, 100 ℃, 250 ℃, 500 ℃, 700 ℃, 800 ℃, 900 ℃ or up to 1131 ℃ of heat of locating, this depends on the material that uses in the heater.
Compare with the heater of constant watt, temperature-limiting heater allows more thermojet to go into the rock stratum, and it is limited to be adapted near the low heat conductivity zone the heater that reason is that the energy of input temperature-limiting heater need not.For example, in green river oil shale, the thermal conductivity of minimum rich oil rammell and the highest rich oil rammell exists factor and is at least 3 difference.When this rock stratum of heating, to compare with the conventional heater of the temperature that is subject to the low heat conductivity layer, temperature-limiting heater obviously is delivered to the rock stratum with more heat.Need be adapted to the low heat conductivity layer so that heater is can be at low heat conductivity layer place not overheated and burn along the thermal output of the whole length of conventional heater.For temperature-limiting heater, near the thermal output of low heat conductivity layer that is in high temperature will reduce; But temperature-limiting heater is not in the remainder of high temperature high thermal output will be provided still.Because be used for the heater of heat hydrocarbon rock stratum have usually very long length (for example at least 10m, 100m, 300m, at least 500m, 1km or up to about 10km), the major part of the length of temperature-limiting heater can be lower than operation under the Curie temperature simultaneously only several sections be in temperature-limiting heater the Curie temperature place or near.
Use temperature-limiting heater to make heat be delivered to the rock stratum effectively.Effective conveying of heat makes the rock stratum is heated to the required time decreased of preferred temperature.For identical heater interval, the temperature that temperature-limiting heater can allow bigger evenly heat output to keep heater device simultaneously is lower than the Equipment Design limit temperature.With comparing than the harmonic(-)mean thermal output of constant watt heater, the pyrolysis in the rock stratum can take place in the time early under by the big evenly heat output that temperature-limiting heater provided.Temperature-limiting heater is offset because the too close inaccurate well interval or the caused focus of holing of heater well.In certain embodiments, the power output that the temperature-limiting heater permission increases after a period of time for the heater well of too far apart, perhaps limited power is exported for too near at interval heater well.The temperature-limiting heater power that also supply is bigger near the zone of cap rock and underlying stratum is to compensate these regional temperature losses.
Temperature-limiting heater advantageously can be used in the rock stratum of a lot of types.For example; Contain in the rock stratum of heavy hydrocarbon in sand asphalt rock stratum or permeable relatively, the low temperature output that temperature-limiting heater can be used to provide controlled with the viscosity that reduces fluid, move fluid and/or improve fluid the pit shaft place or near or Radial Flow in the rock stratum.Temperature-limiting heater can be used to suppress cause excessive green coke to form owing to the rock stratum near the overheated of shaft area.
In certain embodiments, the use of temperature-limiting heater is avoided or has been reduced the needs for expensive temperature-control circuit.For example, the use of temperature-limiting heater is avoided or has been reduced and carried out the needs of thermograph and/or on heater, use the stationary heat galvanic couple to monitor the potential overheated needs in focus place.
In certain embodiments, temperature-limiting heater with regard to manufacturing than standard heater more economically.Typical ferrimagnet comprises iron, carbon steel or ferritic stainless steel.These materials be generally used for nickel-base alloy heating wire in insulated electric conductor (mineral insulated cable) heater (such as nichrome, Kanthal TM(Bulten-Kanthal AB, Sweden) and/or LOHM TM(Driver-Harris company, Harrison, New Jersey, the U.S.)) compare very cheap.In an embodiment of temperature-limiting heater, temperature-limiting heater is fabricated to insulated conductor heater to reduce cost and to improve reliability with continuous length.
Temperature-limiting heater can be used to heat hydrocarbon-containing formation, includes but not limited to oil shale, coal seam, sand asphalt rock stratum and heavy viscous oil.Temperature-limiting heater also can be used for environment and corrects the field with evaporation or destruction soil pollution.The embodiment of temperature-limiting heater can be used to heat fluid in pit shaft or the submerged pipeline to suppress the deposition of paraffin or various hydrates.In certain embodiments, temperature-limiting heater is used for the solution mining in subterranean strata (for example, oil shale or coal seam).In certain embodiments, fluid (for example, the salt of fusion) is arranged in the pit shaft and heats with the distortion that suppresses pit shaft and/or subside with temperature-limiting heater.In certain embodiments, temperature-limiting heater is attached to sucker rod or the parts of sucker rod itself in the pit shaft.In certain embodiments, temperature-limiting heater is used for heating the pit shaft near zone and is transported near the oil viscosity the pit shaft during the ground to reduce high viscosity oil production period and sticky oil.In certain embodiments, make can be through reducing the gas lift that oil viscosity realizes viscous oil not making under the oil cokeization for temperature-limiting heater.Temperature-limiting heater can be used for the sulphur feed-line with temperature maintenance between about 110 ℃ and about 130 ℃.
Some embodiment of temperature-limiting heater can be used for requirement and is controlled at than the chemistry of the rising temperature in the narrow temperature scope or refinery practice to suppress undesirable chemical reaction or the caused infringement because local temperature raises.Some application can include but not limited to reaction tube, coker and destilling tower.Temperature-limiting heater also can be used for pollution control equipment (for example catalytic converter and oxidator) to allow not having to quickly heat up to the control temperature under the complicated temperature-control circuit.In addition, temperature-limiting heater can be used in the food processing to avoid excessive temperature infringement food.Temperature-limiting heater also can be used for the heat treatment (for example, the annealing of solder joint) of metal.Temperature-limiting heater also can be used for floor heater, etcher and/or various other utensil.Temperature-limiting heater can make with biopsy needle and be used for eliminating tumour through the temperature in the rising body.
Some embodiment of temperature-limiting heater can be used in the medical science and/or veterinary equipment of some type.For example, temperature-limiting heater can be used to therapeutic ground and handles the tissue of the mankind or animal.The temperature-limiting heater that is used for medical science or veterinary equipment can have ferrimagnet, comprises that Curie temperature is about 50 ℃ palladium-copper alloy.High frequency (for example greater than approximately the frequency of 1MHz) can be used to drive the relatively little temperature-limiting heater that is used for medical science and/or veterinary use.
The Curie temperature that is used for the ferromagnetic alloy decision heater of temperature-limiting heater.The curie temperature data of various metals is listed in " AIP's handbook ", and (second edition, 5-170 McGraw-Hill) is in the 5-176 page or leaf.Ferromagnetic conductor can comprise the alloy of one or more ferromagnetic elements (iron, cobalt and nickel) and/or these elements.In certain embodiments; Ferromagnetic conductor comprises siderochrome (Fe-Cr) alloy (for example HCM12A and the SAVE12 (SumitomoMetals Co., Japan) and/or contain the ferroalloy (for example Fe-Cr alloy, Fe-Cr-W alloy, Fe-Cr-V (vanadium) alloy, Fe-Cr-Nb (niobium) alloy) of chromium of tungstenic (W).In three kinds of main ferromagnetic components, iron has about 770 ℃ Curie temperature; Cobalt (Co) has about 1131 ℃ Curie temperature; Has about 358 ℃ Curie temperature with nickel.The Curie temperature of ferrocobalt is higher than the Curie temperature of iron.For example, the ferrocobalt that has 2% a weight ratio cobalt has about 800 ℃ Curie temperature; Ferrocobalt with 12% weight ratio cobalt has about 900 ℃ Curie temperature; And the ferrocobalt with 20% weight ratio cobalt has about 950 ℃ Curie temperature.The Curie temperature of iron-nickel alloy is lower than the Curie temperature of iron.For example, the iron-nickel alloy that has 20% weight ratio nickel has about 720 ℃ Curie temperature; And the iron-nickel alloy with 60% weight ratio nickel has about 560 ℃ Curie temperature.
Be used as the Curie temperature of some non-ferromagnetic elements rising iron of alloy.For example, the ferrovanadium that has 5.9% a weight ratio vanadium has about 815 ℃ Curie temperature.Other non-ferromagnetic elements (for example carbon, aluminium, copper, silicon and/or chromium) can with iron or other ferrimagnet alloying to reduce Curie temperature.Thereby the non-ferromagnetic elements of rising Curie temperature is can be with the non-ferromagnetic elements that reduces Curie temperature combined and produce the material with expectation Curie temperature and other expectation physics and/or chemical property with iron or other ferrimagnet alloying.In certain embodiments, curie temperature material is a ferrite, such as NiFe 2O 4In other embodiments, curie temperature material is a binary compound, such as FeNi 3Or Fe 3Al.
Some embodiment of temperature-limiting heater can comprise more than a kind of ferrimagnet.If any situation described here is applicable at least a ferrimagnet in the temperature-limiting heater, these embodiment are in the scope of embodiment described here.
Ferromagnetism character can fail along with asymptotic Curie temperature usually." industrial electro heating handbook " (U.S. electric and publishing house of Electronic Engineering Association, 1995) of C.James Erickson show the typical curve of 1% carbon steel (carbon with 1% weight ratio).The temperature place that is higher than 650 ℃ that is lost in of permeability begins and tends to when temperature surpasses 730 ℃, to finish.Thereby, the actual Curie temperature from limit temperature a shade below ferromagnetic conductor.The depth of penetration of electric current at room temperature locates to increase to 0.445cm for 0.132cm and at 720 ℃ in 1% carbon steel.From 720 ℃ to 730 ℃, the depth of penetration increases to above 2.5cm sharp.Thereby, utilize the embodiment of the temperature-limiting heater of 1% carbon steel between 650 ℃ and 730 ℃, to begin from restriction.
The depth of penetration defines effective length of penetration of the electric current entering conductive material of time variation usually.Generally, current density reduces along with pressing index law ground along the radius of conductor from the distance at external surface to center.Current density is that the degree of depth of the about 1/e part of surface current density is called the depth of penetration.For the solid cylindrical bar of diameter much larger than the depth of penetration, perhaps wall thickness surpasses the hollow cylinder of penetration depth, and depth of penetration δ is:
(1)δ=1981.5*(ρ/(μ*f)) 1/2
Wherein: δ=in the depth of penetration of inch;
Resistivity under ρ=operating temperature (ohm-cm);
μ=relative permeability; With
F=frequency (Hz).
Formula 1 obtains from " industrial electro heating handbook " (U.S. electric and publishing house of Electronic Engineering Association, 1995) of C.James Erickson.For most metal, resistivity (ρ) increases along with temperature.Relative permeability is usually along with temperature and electric current and change.Other formula can be used to estimate that the permeability and/or the depth of penetration are about temperature and/or change in current.μ stems from the dependence of μ to magnetic field to the dependence of electric current.
The material that is used for temperature-limiting heater can select to provide the conditioning desired ratio.Temperature-limiting heater can be selected the adjusting ratio of 1.1: 1,2: 1,3: 1,4: 1,5: 1,10: 1,30: 1 or 50: 1 at least.Also can use bigger adjusting ratio.Selected adjusting ratio can be depending on several factors; Include but not limited to arrange the type (for example higher adjusting is than can be used for the oil shale layer that thermal conductivity between richness and the lean oil shale layer has great changes) of the rock stratum of temperature-limiting heater and/or be used for the temperature limitation (for example, the temperature limitation of heater material) of the material of pit shaft.In certain embodiments, regulate than through will extra copper or other good electric conductor be bonded to ferrimagnet and increase (for example, adding copper) with the resistance on the reduction Curie temperature.
Temperature-limiting heater can be lower than the thermal output (power output) that provides minimum under the Curie temperature of heater.In certain embodiments, minimum thermal output is for 400W/m at least (watt every meter), 600W/m, 700W/m, 800W/m or up to 2000W/m.When the temperature of a heater part was close to or higher than Curie temperature, temperature-limiting heater reduced the amount of thermal output through this part of heater.The heat that reduces can be significantly less than the thermal output that is lower than under the Curie temperature.In certain embodiments, the heat of reduction is maximum 400W/m, 200W/m, 100W/m perhaps can be near 0W/m.
The AC of temperature-limiting heater or modulation DC resistance and/or thermal output can reduce along with the temperature asymptotic Curie temperature, and since curie effect and near the Curie temperature or on reduce sharp.In certain embodiments, on the Curie temperature or maximum certain numerical value half the of resistance or the thermal output at place a bit of the numerical value of near resistance or thermal output for being lower than Curie temperature.In certain embodiments, be higher than near Curie temperature or the Curie temperature thermal output a bit (for example is lower than 30 ℃ of Curie temperature, is lower than 40 ℃ of Curie temperature, is lower than 50 ℃ of Curie temperature or is lower than 100 ℃ of Curie temperature) thermal output located at most for certain that is lower than Curie temperature 90%, 70%, 50%, 30%, 20%, 10% or still less (low) to 1%.In certain embodiments, be higher than near Curie temperature or the Curie temperature resistance drop and be low to moderate 80%, 70%, 60%, 50% or still less (low) that certain that be lower than Curie temperature a bit (for example is lower than 30 ℃ of Curie temperature, is lower than 40 ℃ of Curie temperature, is lower than 50 ℃ of Curie temperature or is lower than 100 ℃ of Curie temperature) resistance located to 1%.
In certain embodiments, regulate the AC frequency to change the depth of penetration of ferrimagnet.For example, the depth of penetration under the 1% carbon steel room temperature is 0.132cm when 60Hz, is 0.0762cm when 180Hz, and is 0.046cm when 440Hz.Because the diameter of heater is usually greater than the twice of the depth of penetration, so utilize higher frequency (and thereby heater have littler diameter) to reduce the heater cost.For fixing geometry, higher frequency has produced higher adjusting ratio.Adjusting under the upper frequency is than calculating through comparing with the adjusting lower frequency under to multiply each other divided by the square root of lower frequency with upper frequency.In certain embodiments, use between 100Hz and the 1000Hz, between 140Hz and the 200Hz or the frequency (for example 180Hz, 540Hz or 720Hz) between 400Hz and the 600Hz.In certain embodiments, can use high frequency.Frequency can be greater than 1000Hz.
In certain embodiments, modulation DC (for example slicing DC, waveform modulated DC or circulation DC) can be used to electric energy is offered temperature-limiting heater.DC modulator or DC peak clipper can be bonded to the DC power supply so that the direct current output of modulation is provided.In certain embodiments, the DC power supply can comprise the device that is used to modulate DC.An example of DC modulator is DC to a DC converting system.DC to DC converting system is commonly known in the art.DC modulated or slicing usually becomes expected waveform.Be used for the DC modulated waveform and comprise square wave, sine wave, distortion sinusoidal wave, distortion square wave, triangle and Else Rule or irregular waveform, but be not limited thereto.
Modulation DC waveform defines the frequency of modulation DC usually.Thereby modulation DC waveform can select to provide the modulation DC frequency of expectation.The shape of modulation DC waveform and/or modulation rate (such as slicing speed) can change to change modulation DC frequency.DC can be modulated under the frequency that is higher than common available AC frequency.For example, modulation DC can provide under the frequency of 1000Hz at least.The frequency of supply electric current is increased to the adjusting ratio that high value has advantageously increased temperature-limiting heater.
In certain embodiments, adjusting or change modulation DC waveform are with the frequency of change modulates DC.The DC adjuster can be regulated under high electric current or high pressure or change and modulate the DC waveform in any time between the operating period of temperature-limiting heater.Thereby the modulation DC that offers temperature-limiting heater is not limited to single-frequency or even the frequency values of a group.Use the waveform of DC modulator to select the common discrete control that allows modulation DC frequency with the modulation DC frequency of wide region.Thereby modulation DC frequency is easier to be arranged on a clear and definite value and the AC frequency is restricted to the multiple of frequency of supply usually.The discrete control of modulation DC frequency allows the more optionally control of adjusting ratio for temperature-limiting heater.The material of wide region is used for the design of temperature-limiting heater and constructs than allowing more optionally to control the warm adjusting of heating of limit.
In certain embodiments, temperature-limiting heater comprises the composite conductor of the high conductivity core with ferromagnetism pipe and nonferromagnetic.The high conductivity core of nonferromagnetic has reduced the required diameter of conductor.The conductor of core or nonferromagnetic can be copper or copper alloy.The conductor of core or nonferromagnetic also can be by having low-resistivity and processing near other metal of 1 relative permeability (for example, the material of nonferromagnetic basically is such as aluminium and aluminium alloys, phosphor bronze, beallon and/or brass).Composite conductor allows the resistance of temperature-limiting heater near Curie temperature, to reduce more tempestuously.Along with the depth of penetration increases near Curie temperature to comprise the copper core, resistance reduces very tempestuously.
Composite conductor can increase the electrical conductivity of temperature-limiting heater and/or allow heater under lower voltage, to move.In one embodiment, composite conductor has flat relatively resistance-temperature curve at the temperature place of the Curie temperature near zone of the ferromagnetic conductor that is lower than composite conductor.In certain embodiments, temperature-limiting heater has between the flat relatively resistance-temperature curve between 100 ℃ and 750 ℃ or between 300 ℃ and 600 ℃.Flat relatively resistance-temperature curve also can be presented in other temperature range through material and/or the configuration of regulating in the temperature-limiting heater for example of material.In certain embodiments, in the composite conductor relative thickness of every kind of material select the feasible resistance-temperature curve that produces expectation for temperature-limiting heater.
In certain embodiments, in the composite conductor relative thickness of every kind of material select the feasible resistance-temperature curve that produces expectation for temperature-limiting heater.
Composite conductor (for example, compound inner conductor or compound outer contact) can be made through the method that includes but not limited to following method: co-extrusion, rollforming, the tubulature that closely cooperates (cooled interior element and heat outer member for example; Then inner member is inserted outer member; After this carry out the drawing operation and/or allow system cools); Blast or electromagnetism coat; Electric arc covers welding; The taeniae welding; The plasma powder welding; The billet co-extrusion; Electroplate; Drawing; Sputter; Plasma deposition; The co-extrusion casting; Magnetic is shaped; Fusion cylinder casting (inner core material core material outside is interior or opposite); Weld after inserting or the high temperature steaming; Shielding active gases welding (SAG); And/or after inserting interior pipe in the outer tube through hydroforming or use the pig iron come mechanically to expand in pipe with respect to outer dilator tube with forge in pipe.In certain embodiments, ferromagnetic conductor is woven on the nonferromagnetic conductor.In certain embodiments, the composite conductor utilization is similar to those methods that are used to coat and forms (for example, using copper-clad steel).Metallurgical binding between copper-clad coating and the iron matrix magnetic material can be favourable.Composite conductor through the coextrusion process that forms good metallurgical binding (the for example good combination between copper and 446 stainless steels) produces can be by Anomet Products, and Inc. (State of Massachusetts, US Shrewsbury) provides.
Fig. 3-5 shows the various embodiment of temperature-limiting heater.One or more characteristics of the embodiment of the temperature-limiting heater shown in any one can be combined with one or more characteristics of other embodiment of these temperature-limiting heaters shown in the drawings in these accompanying drawings.Among described here some embodiment, being designed and sized under the AC of 60Hz frequency of temperature-limiting heater moves.It is to be understood that the size of temperature-limiting heater can be regulated so that temperature-limiting heater can move down under other AC frequency or at modulation DC electric current in a similar fashion by described here those.
Be lower than for the temperature-limiting heater that most resistive thermal output is provided under the Curie temperature for ferromagnetic conductor wherein, most of electric current is crossed material with magnetic field (H) with magnetic induction intensity (B) high nonlinearity function flow.These nonlinear functions can cause strong inductive effect and the distortion that causes temperature-limiting heater to reduce in the temperature place power factor that is lower than Curie temperature.These effects can cause the supply of electric power of temperature-limiting heater to be difficult to control and can cause extra electric current to flow through the surface and/or increase the weight of the load of power conductor.System's (such as variable condenser or modulation power source) expensive and/or that be difficult to apply control can be used to attempt to compensate these effects and controls wherein most resistive thermal output by the temperature-limiting heater that electric current provided that flows through ferrimagnet.
In the embodiment of some temperature-limiting heater, ferromagnetic conductor defines at temperature-limiting heater and is lower than the Curie temperature of ferromagnetic conductor or near most of electric current of the electric conductor through being bonded to ferromagnetic conductor this temperature the time.Electric conductor can be sheath, overcoat, support component, corrosion-resistant element or other resistance element.In certain embodiments, ferromagnetic conductor defines the most of electric current that flows to the electric conductor that is positioned between outermost layer and the ferromagnetic conductor.Ferromagnetic conductor be positioned in the cross section of temperature-limiting heater so that the magnetic confinement of ferromagnetic conductor when being lower than Curie temperature or be in this temperature flow to most of electric current of electric conductor.Most of electric current is owing to the kelvin effect of ferromagnetic conductor is limited to electric conductor.Thereby most of electric current electrical resistance property with substantial linear in most opereating specification of heater flows through material.
In certain embodiments, ferromagnetic conductor and electric conductor are positioned in the cross section of temperature-limiting heater so that the kelvin effect of ferromagnetic conductor when being lower than the temperature of Curie temperature limited the penetration depth of the electric current in electric conductor and the ferromagnetic conductor.Thereby, electric conductor temperature reach ferromagnetic conductor the Curie temperature place or near provide temperature-limiting heater most resistive thermal output.In certain embodiments, the size of electric conductor may be selected to be provides the thermal output of expectation character.
Because most of electric current flows through the electric conductor that is lower than Curie temperature, temperature-limiting heater has a resistance-temperature curve, and this curve has reflected the resistance-temperature curve of material in the electric conductor at least in part.Thereby if the material in the electric conductor has the resistance-temperature curve of substantial linear, the resistance-temperature curve of temperature-limiting heater is substantial linear when being lower than the Curie temperature of ferromagnetic conductor.The resistance of temperature-limiting heater seldom or not depend on flow through heater electric current up to the temperature asymptotic Curie temperature.Most of electric current flows in electric conductor when being lower than Curie temperature but not in ferromagnetic conductor, flows.
Resistance-the temperature curve of the temperature-limiting heater that wherein most of electric current flows in electric conductor also tends near the Curie temperature of ferromagnetic conductor or this temperature place shows more acutely reducing of resistance.Near the Curie temperature or this temperature place resistance more acutely reduce than Curie temperature near more progressive resistance reduce and be easier to control.
In certain embodiments, being sized to of material in the electric conductor and/or material makes temperature-limiting heater when being lower than the Curie temperature of ferromagnetic conductor, have the resistance-temperature curve of expectation.
Wherein most of electric current when being lower than Curie temperature, in electric conductor, flow but not in ferromagnetic conductor the temperature-limiting heater of fluid be easier to prediction and/or control.Wherein most of electric current flows in electric conductor when being lower than Curie temperature but not the activity of the temperature-limiting heater that in ferromagnetic conductor, flows can be predicted through for example its resistance-temperature curve and/or its power factor-temperature curve.Resistance-temperature curve and/or power factor-temperature curve can be estimated or predict through for example estimating analysis formula that the movable experiment measuring of temperature-limiting heater, estimation or prediction temperature-limiting heater are movable and/or estimation or the movable simulation of prediction temperature-limiting heater.
In certain embodiments, the activity of estimation or prediction temperature-limiting heater is used for controlling temperature-limiting heater.Temperature-limiting heater can be controlled based on the measurement (estimation) of heater run duration resistance and/or power factor.In certain embodiments, power or the electric current that is supplied to temperature-limiting heater estimated to compare with the expected activity of heater based on the estimation of heater run duration resistance and/or power factor and with this and controlled.In certain embodiments, temperature-limiting heater is controlled under the temperature near HEATER FOR MEASURING temperature or the heater not having.Do not avoided measuring relevant running cost there being under the temperature survey control temperature-limiting heater with downhole temperature.With compare based on measuring temperature control heater, control temperature-limiting heater based on the estimation of the resistance of heater and/or power factor and also reduced the time that the power that is supplied to heater or electric current are regulated.
The temperature of temperature-limiting heater near or when surpassing the Curie temperature of ferromagnetic conductor, ferromagnetic reduction allows electric current to flow through the more most conduction cross section of temperature-limiting heater in the ferromagnetic conductor.Thereby, the Curie temperature place of ferromagnetic conductor or near, the resistance of temperature-limiting heater reduces and temperature-limiting heater automatically provides the thermal output of reduction.In certain embodiments, combination of elements to the ferromagnetic conductor of high conduction and electric conductor with the reduction temperature-limiting heater at the Curie temperature place of ferromagnetic conductor or the resistance when being higher than this temperature.The element of high conduction can be another conductor element of inner conductor, core or copper, aluminium, nickel or its alloy.
Provide the ferromagnetic conductor in the temperature-limiting heater of most resistive thermal output to compare with near reaching Curie temperature or this temperature, using ferromagnetic conductor, the ferromagnetic conductor that when temperature is lower than Curie temperature, most of electric current is limited to electric conductor can have relatively little cross section.Use electric conductor when being lower than Curie temperature, to provide the temperature-limiting heater of most resistive thermal output when temperature is lower than Curie temperature, to have low magnetic induction coefficient; Because most resistive thermal output is compared by the temperature-limiting heater that ferrimagnet provides when wherein being lower than Curie temperature, less electric current flows through ferromagnetic conductor.Ferromagnetic conductor radius (r) magnetic field of locating (H) and the electric current that flows through ferromagnetic conductor and core (I) are directly proportional divided by radius, perhaps
(2)H∝I/r
Because only one part of current flows through ferromagnetic conductor for the use outer contact provides most resistive thermal output when being lower than Curie temperature temperature-limiting heater, the magnetic field of temperature-limiting heater can be significantly less than the magnetic field that wherein most of electric current flows through the temperature-limiting heater of ferrimagnet.For little magnetic field, relative permeability (μ) can be very big.
The depth of penetration of ferromagnetic conductor (δ) is inversely proportional to the square root of relative permeability (μ):
(3)δ∝(1/μ) 1/2
Increase the depth of penetration that relative permeability can reduce ferromagnetic conductor.Yet; Because only one part of current flows through ferromagnetic conductor for the temperature that is lower than Curie temperature; For the bigger ferrimagnet of relative permeability, the radius of ferromagnetic conductor (or thickness) can reduce the depth of penetration that reduces with compensation and still allow kelvin effect to be limited in the penetration of current that temperature is lower than the Curie temperature place electric conductor of ferromagnetic conductor simultaneously.The radius of ferromagnetic conductor (thickness) can be between between 0.3mm and the 8mm, between 0.3mm and the 2mm or between 2mm and the 4mm, this depends on the relative permeability of ferromagnetic conductor.The thickness that reduces ferromagnetic conductor can reduce the manufacturing cost of temperature-limiting heater because the cost of ferrimagnet to tend to be the major part of cost of temperature-limiting heater.The Curie temperature place of ferromagnetic conductor or near, the relative permeability that increases ferromagnetic conductor be temperature-limiting heater provide higher adjusting than with the more acutely reduction of resistance.
Relative permeability higher (for example at least 200, at least 1000, at least 1 * 10 4Perhaps at least 1 * 10 5) and/or the ferrimagnet (such as pure iron or ferrocobalt) of Curie temperature higher (for example at least 600 ℃, at least 700 ℃ or at least 800 ℃) tend at high temperature have less corrosion resistance and/or less mechanical strength.Electric conductor can be temperature-limiting heater corrosion resistance and/or high mechanical strength under the high temperature is provided.Thereby ferromagnetic conductor can be mainly its ferromagnetism and select.
When being lower than the Curie temperature of ferromagnetic conductor, most of electric current is restricted to the variation that electric conductor has reduced power factor.Because only one part of current flows through ferromagnetic conductor when being lower than Curie temperature, the nonlinear ferroelectric magnetic property of ferromagnetic conductor very little or do not have for the influence of the power factor of temperature-limiting heater at all, except the Curie temperature place or near.Even the Curie temperature place or near, with wherein when being lower than Curie temperature ferromagnetic conductor provide the temperature-limiting heater of most resistive thermal output to compare, the influence of power factor is also reduced.Thereby, seldom need or do not need external compensation (for example variable condenser or waveform modulated) to regulate variation in the inductive load of temperature-limiting heater to keep high relatively power factor.
In certain embodiments, the temperature-limiting heater holding power factor between the operating period of heater that when being lower than the Curie temperature of ferromagnetic conductor, most of electric current is restricted to electric conductor is higher than 0.85, be higher than 0.9 or be higher than 0.95.Any reduction of power factor only takes place near the part that is in temperature-limiting heater of the temperature Curie temperature.Big many parts of temperature-limiting heater be not in usually during use the Curie temperature place or near.These parts have the High Power Factor near 1.0.The power factor of whole temperature-limiting heater is maintained between the operating period of heater and is higher than 0.85, is higher than 0.9 or be higher than 0.95, is lower than 0.85 power factor even the some parts of heater has.
Keep high power factor and also allow more cheap power supply and/or control appliance, such as solid-state power source or SCR (thyristor).If power factor is owing to inductive load changes too greatly, these equipment possibly just can not correctly move so.Yet when power factor maintained high value, these equipment can be used to power is offered temperature-limiting heater.Solid-state power source also has the advantage that allows meticulous adjustment and controlled adjustment to be supplied to the power of temperature-limiting heater.
In certain embodiments, with transformer power is offered temperature-limiting heater.Transformer can have the multivoltage joint so that power is offered temperature-limiting heater.The multivoltage joint allows the electric current of supply between a plurality of voltages, to switch back and forth.This maintains electric current in the scope by the multivoltage joint restraint.
High conducting element or inner conductor have increased the adjusting ratio of temperature-limiting heater.In certain embodiments, the thickness that increases high conducting element is to increase the adjusting ratio of temperature-limiting heater.In certain embodiments, the thickness that reduces electric conductor is to increase the adjusting ratio of temperature-limiting heater.In certain embodiments, the adjusting of temperature-limiting heater than between between 1.1 and 10, between between 2 and 8, or between 3 and 6, (for example regulate than be at least 1.1, be at least 2, perhaps be at least 3).
In certain embodiments, with the conductive layer of relative thin come temperature reach ferromagnetic conductor Curie temperature or near the time most resistive thermal output of temperature-limiting heater is provided.This temperature-limiting heater can be used as the heating element in the insulated conductor heater.Heating element in the insulated conductor heater can be positioned at sheath, has insulating layer between this sheath and the heating element.
Fig. 3 A and 3B show with the viewgraph of cross-section of temperature-limiting heater as an embodiment of the insulated conductor heater of heating element.Insulated electric conductor 212 comprises core 214, ferromagnetic conductor 216, inner conductor 218, electrical insulator 220 and shell 222.Core 214 is copper cores.Ferromagnetic conductor 216 is for example iron or ferroalloy.
The conductive layer of the relative thin of inner conductor 218 nonferromugnetic material that to be electrical conductivity higher than ferromagnetic conductor 216.In certain embodiments, inner conductor 218 is a copper.Inner conductor 218 also can be a copper alloy.Copper alloy has the resistance-temperature curve more flat than fine copper usually.More flat resistance-temperature curve can be provided at when reaching Curie temperature variation littler in the thermal output as temperature funtion.In certain embodiments, inner conductor 218 is copper (for example, CuNi6 or the LOHM with 6% weight ratio nickel TM).In certain embodiments, inner conductor 218 is CuNi10Fe1Mn alloys.When being lower than the Curie temperature of ferromagnetic conductor 216, the magnetic of ferromagnetic conductor is restricted to inner conductor 218 with most of electric current.Thereby inner conductor 218 provides most resistive thermal output of insulated electric conductor 212 when being lower than Curie temperature.
In certain embodiments, inner conductor 218 is with core 214, ferromagnetic conductor 216 design sizes, so that inner conductor provides the heat output and the conditioning desired ratio of expectation.For example, inner conductor 218 can have less than about 2 to the 3 times cross-sectional area of core 214 cross-sectional areas.Usually, inner conductor 218 must have relatively little cross-sectional area so that the thermal output of expectation to be provided, if inner conductor is copper or copper alloy.At inner conductor 218 is among the embodiment of copper; Core 214 has the diameter of 0.66cm, and ferromagnetic conductor 216 has the external diameter of 0.91cm, and inner conductor 218 has the external diameter of 1.03cm; Electrical insulator 220 has the external diameter of 1.53cm, and shell 222 has the external diameter of 1.79cm.At inner conductor 218 is among the embodiment of CuNi6; Core 214 has the diameter of 0.66cm, and ferromagnetic conductor 216 has the external diameter of 0.91cm, and inner conductor 218 has the external diameter of 1.12cm; Electrical insulator 220 has the external diameter of 1.63cm, and shell 222 has the external diameter of 1.88cm.This insulated electric conductor is usually than not using thin inner conductor when being lower than Curie temperature, to provide the insulated electric conductor of most thermal output littler and manufacturing cost is more cheap.
Electrical insulator 220 can be magnesia, alumina, silica, beryllium oxide, boron nitride, silicon nitride or its combination.In certain embodiments, electrical insulator 220 is magnesian compacted powder.In certain embodiments, electrical insulator 220 comprises silicon nitride particle.
In certain embodiments, a substratum material arrangements at high temperature migrates into electrical insulator to suppress copper between electrical insulator 220 and inner conductor 218.For example, substratum nickel (for example, the nickel of about 0.5mm) can be arranged between electrical insulator 220 and the inner conductor 218.
Overcoat 222 is processed by resistant material, is such as but not limited to 347 stainless steels, 347H stainless steel, 446 stainless steels, or 825 stainless steels.In certain embodiments, overcoat 222 the Curie temperature place of ferromagnetic conductor 216 or on for insulated electric conductor 212 certain mechanical strength is provided.In certain embodiments, overcoat 222 is not used in conductive electric current.
In some embodiment of temperature-limiting heater, three temperature-limiting heaters combine with three-phase y structure.Three temperature-limiting heaters are combined the electric current that has reduced in each temperature-limiting heater with three-phase y structure, because electric current is split branch between three heaters.The electric current that reduces in each temperature-limiting heater allows each heater to have little diameter.Low electric current allows higher relative permeability in each temperature-limiting heater, and has therefore allowed higher adjusting ratio.In addition, each temperature-limiting heater need not return current.Thereby, having its oneself return current path with each temperature-limiting heater and compare, the adjusting of each temperature-limiting heater is more higher than still.
In three-phase y structure, each temperature-limiting heater can combine through the current-carrying part (conductor of heat is provided) that sheath, shell or the jar of each temperature-limiting heater is shorted to its terminal (for example heater is in the end of heater wellbore at).In certain embodiments, sheath, shell, jar and/or current-carrying part are bonded to the support component that in pit shaft, supports temperature-limiting heater.
Fig. 4 A shows the embodiment that is used at pit shaft installation and heater-combining.Embodiment among Fig. 4 A shows the insulated conductor heater that is fit into pit shaft.The heater of other type is installed in the pit shaft such as the illustrated embodiment also capable of using of conductor heater in the pipeline.And, in Fig. 4 A, show two insulated electric conductors 212, and the 3rd insulated electric conductor from shown in view invisible.Usually, three insulated electric conductors 212 will be bonded to support component 224, shown in Fig. 4 B.In one embodiment, support component 224 is 347H pipes of heavy wall.In certain embodiments, thermoelectricity occasionally other temperature pick up be arranged in the support component 224.Three insulated electric conductors can combine by three-phase y structure.
In Fig. 4 A, insulated electric conductor 212 is coiled on the coiling tube 226.When installing on 226 unwinding, insulated electric conductor is bonded to support component 224 at insulated electric conductor 212.In certain embodiments, insulated electric conductor 212 unwinding and/or side by side be bonded to support component 224 side by side.Insulated electric conductor 212 metals capable of using (for example 304 stainless steels or
Figure GSB00000585593000261
alloy) band 228 is bonded to support component 224.In certain embodiments, insulated electric conductor 212 utilizes the securing member (such as bracelet, wire clamp or snapper) of other type to be bonded to support component 224.Support component 224 is installed in the opening 230 together with insulated electric conductor 212.In certain embodiments, insulated electric conductor 212 combines under the condition of not using support component.For example, one or more bands 228 can be used to insulated electric conductor 212 is combined.
Insulated electric conductor 212 can be in the lower end electricity combination (for example, for three-phase y structure) each other of insulated electric conductor.In three-phase y structure, insulated electric conductor 212 moves under the situation of current loop not having.In certain embodiments, insulated electric conductor 212 section 232 electricity combination each other in the contact.At section 232, electric each other combination of sheath, shell, jar and/or conductive section and/or electricity are bonded to support component 224 so that insulated electric conductor 212 electricity in this section combines.
In certain embodiments, the sheath of insulated electric conductor 212 is shorted to the conductor of insulated electric conductor.Fig. 4 C shows the embodiment that sheath is shorted to the insulated electric conductor 212 of conductor.Sheath 222 utilizes terminal 233 electricity to be bonded to core 214, ferromagnetic conductor 216 and inner conductor 218.Terminal 233 can be metal band or the metal sheet that is positioned at insulated electric conductor 212 lower ends.For example, terminal 233 can be to be bonded to the copper coin of sheath 222, core 214, ferromagnetic conductor 216 and inner conductor 218 so that they are by short circuit.In certain embodiments, terminal 233 is soldered or is brazed to sheath 222, core 214, ferromagnetic conductor 216 and inner conductor 218.
But the sheath short circuit of each insulated electric conductor 212 gets up and combines the conductor of insulated electric conductor with electricity, shown in Fig. 4 A and 4B.In certain embodiments, but the sheath short circuit get up because sheath physics contact to each other.For example, if when sheath is stopped up by band 228, but the contact of sheath physics.In certain embodiments, before insulated electric conductor 212 was installed in the opening, the lower end of sheath physically combined (for example welding) at the place, ground of opening 230.
In certain embodiments, three conductors are positioned in the single pipeline to form the heater that has three conductors in the pipeline.Fig. 5 A and 5B show an embodiment of the heater that has three conductors in the pipeline.Fig. 5 A shows the top-down view of the heater that has three conductors in the pipeline.Fig. 5 B shows the lateral view of the heater that has three conductors in the pipeline, wherein has otch so that its inside to be shown.Three conductors 234 are positioned in the pipeline 236.Three conductors 234 in pipeline 236 basically equably at interval.In certain embodiments, three conductors 234 combine with the helicity structure.
One or more centralizers 238 are arranged in around each conductor 234.Centralizer 238 is processed by electrically insulating material, such as silicon nitride or boron nitride.Centralizer 238 is kept the position of conductor 234 in pipeline 236.Centralizer 238 is also forbidden electrically contacting between conductor 234 and the pipeline 236.In certain embodiments, centralizer 238 is opened so that surround the centralizer of a conductor and the centralizer overlapping (seeing in the top-down view) of another conductor along the intervals of lengths of conductor 234.The tight spacing that this has reduced the required centralizer number of each conductor and has allowed conductor.
In certain embodiments, three conductors 234 combine with three-phase y structure.Three conductors 234 can three-phase y structure be combined in heater at or near.In three-phase y structure, pipeline 236 does not have electricity to be bonded to three conductors 234.Thereby pipeline 236 can only be used for intensity being provided and/or suppressing its corrosion to three conductors 234.
In certain embodiments, heating system comprises one or more heaters (for example, primary heater, secondary heater and the 3rd heater), a plurality of electrical insulator and pipeline.Heater, electrical insulator and pipeline can combine and/or couple together to allow to be arranged in the opening in the subterranean strata.Pipeline can surround heater and electrical insulator.In certain embodiments, pipeline is by means of one or more electrical insulators and heater electric insulation.In certain embodiments, the structure of pipeline has suppressed formation fluid entering pipeline.
Each heater of heating system can be surrounded by at least one electrical insulator.Electrical insulator can be opened with the electrical insulator that allows to surround the electrical insulator of a heater and surround another heater laterally overlapping along the intervals of lengths of each heater.In certain embodiments, electrical insulator comprises silicon nitride.
Heater can comprise that electricity is bonded to the ferromagnetic component of electric conductor.Electric conductor can be any electric conductor described here that first thermal output is provided when being lower than the Curie temperature of ferromagnetic component.Electric conductor can allow to pass at about 25 ℃ of following most of electric currents the cross section of heater.At some embodiment, ferromagnetic component and electric conductor are combined so that the power factor of heater still is higher than 0.85 between the operating period of each heater by electricity.
In certain embodiments, ferromagnetic conductor positions with respect to electric conductor.Ferromagnetic conductor allows when temperature is lower than near Curie temperature or this temperature of ferromagnetic conductor, by the electromagnetic field that electric current produced in the ferromagnetic conductor most of electric current to be restricted to electric conductor with respect to electric conductor location.
In certain embodiments, heating system described here allows heat to be passed to a part of subterranean strata from heater.Heating system has about at least 1.1 adjusting ratio.First thermal output when in certain embodiments, heating system described here provides the Curie temperature that (a) be lower than ferromagnetic conductor and (b) the Curie temperature place of about ferromagnetic conductor or on second thermal output.Second thermal output is compared reduction with first thermal output.In certain embodiments, when first thermal output is in when being lower than about 50 ℃ of selected temperature, second thermal output is at most 90% of first thermal output.
In certain embodiments, temperature-limiting heater is used for obtaining the heating (for example, be used for heating the fluid of producing well, the heating surface line perhaps reduces in the pit shaft or the viscosity of fluid in the pit shaft near zone) of lower temperature.The ferrimagnet that changes temperature-limiting heater allows the heating of lower temperature.In certain embodiments, ferromagnetic conductor is processed by the Curie temperature material lower than 446 stainless steels.For example, ferromagnetic conductor can be the alloy of iron and nickel.This alloy can have the nickel between 30% to 42% weight ratio, and all the other are iron.In one embodiment, alloy is Invar36.Invar 36 is the Curie temperature that have the nickel of 36% weight ratio in the iron and have 277 ℃.In certain embodiments, alloy is to have for example three component alloys of chromium, nickel and iron.For example, a kind of alloy can have the chromium of 6% weight ratio, the nickel of 42% weight ratio and the iron of 52% weight ratio.2.5cm the Invar 36 of diameter has about 2 to 1 adjusting ratio under Curie temperature.The Invar36 alloy is arranged in allows littler excellent diameter on the copper core.The copper core can produce high adjusting ratio.When the alloy that is lower than polymer insulation bulk melting point or softening point with Curie temperature used, the isolator among the low-temperature heater embodiment can be processed by high-performance polymer isolator (such as PFA or PEEKTM).
The further modification of various aspects of the present invention and alternative embodiment for the one skilled in the art who sees this description clearly.So this description is regarded as only to be exemplary and to be used to instruct the general manner of one skilled in the art's embodiment of the present invention.Be to be understood that, here shown in described form of the present invention only as presently preferred embodiment.For replacing with described element and material shown in here, parts and technology can be put upside down, and some characteristic of the present invention can utilize independently, and all these all are clearly for the one skilled in the art who has benefited from the present invention's description.Do not deviating under the present invention's spirit and scope as claimed in claim and can change element described here.In addition, it is to be understood that in certain embodiments, the characteristics of independent description are combinable here.

Claims (18)

1. heating system that is used for subterranean strata comprises:
Be arranged in primary heater, secondary heater and the 3rd heater (212) in the opening (230) in the subterranean strata, wherein each heater (212) comprising:
Electric conductor (214; 216; 218);
Surround electric conductor (214 at least in part; 216; 218) electrical insulator (220);
Surround the conductive jacket (222) of electrical insulator (220) at least in part;
Wherein electric conductor (214; 216; 218) end portion (232) electricity in heater (212) is bonded to sheath (222), and said end portion (232) is the part away from open surfaces of heater (212);
Primary heater, secondary heater and the 3rd heater (212) combine at end portion (232) electricity of heater (212); With
Primary heater, secondary heater and the 3rd heater (212) are configured to combine with the three-phase y structure electricity;
Wherein this system also comprises support component, and primary heater, secondary heater and the 3rd heater are bonded to this support component; Wherein electric conductor (214; 216; 218) comprising:
Internal layer electric conductor (214);
Surround internal layer electric conductor (214) and electricity at least in part and be bonded to the ferromagnetic conductor (216) of internal layer electric conductor (214);
Electricity is bonded to the outer electric conductor (218) of ferromagnetic conductor (216); This skin electric conductor (218) surrounds ferromagnetic conductor (216) at least in part, and outer electric conductor (218) is lower than most of resistive thermal output that heater is provided under the about 50 ℃ temperature of selected temperature reaching; With
One or more electrical insulators (220) that surround outer electric conductor (218) at least in part.
2. heating system as claimed in claim 1, wherein ferromagnetic conductor (216) is located such that under near the temperature that is lower than selected temperature or the selected temperature by the electromagnetic field that electric current produced that in ferromagnetic conductor (216), flows most of electric current flow restriction to outer electric conductor (218) with respect to outer electric conductor (218).
3. heating system as claimed in claim 1, wherein heating system is configured provide (a) be lower than first thermal output of selected temperature and (b) greatly about the selected temperature place or on second thermal output, second thermal output is compared reduction with first thermal output.
4. heating system as claimed in claim 2, wherein heating system is configured provide (a) be lower than first thermal output of selected temperature and (b) greatly about the selected temperature place or on second thermal output, second thermal output is compared reduction with first thermal output.
5. heating system as claimed in claim 3, wherein heating system is configured automatically provides second thermal output.
6. heating system as claimed in claim 4, wherein heating system is configured automatically provides second thermal output.
7. like arbitrary described heating system among the claim 3-6, wherein second thermal output is at most that 90%, the first thermal output of first thermal output is located for about 50 ℃ being lower than selected temperature.
8. like arbitrary described heating system among the claim 1-6, wherein internal layer electric conductor (214), ferromagnetic conductor (216) and outer electric conductor (218) electricity combine so that the power factor of heating system still is higher than about 0.85 between the operating period of heater.
9. like arbitrary described heating system among the claim 1-6, wherein selected temperature is the Curie temperature of ferromagnetic conductor (216).
10. like arbitrary described heating system among the claim 1-6, wherein electrical insulator (220) comprises and surrounds electric conductor (214 at least in part; 216; 218) one or more electrical insulators.
11. like arbitrary described heating system among the claim 1-6, wherein heating system has about at least 1.1 adjusting ratio.
12. a method that is used for arbitrary described heating system in subterranean strata is installed like claim 1-11, this method comprises:
The position of the opening in subterranean strata (230) is positioned at primary heater (212) on first bobbin (226), secondary heater (212) is positioned at second bobbin (226) goes up and the 3rd heater (212) is positioned on the 3rd bobbin (226);
In the time of in the said opening (230) that heater (212) is installed in the subterranean strata, with each unwinding of primary heater, secondary heater and the 3rd heater (212);
In the time of in the said opening (230) that heater (212) is installed in the subterranean strata, in conjunction with each heater (212); With
With three-phase y structure electricity heater-combining (212).
13. method as claimed in claim 12, wherein said one or more electrical insulators (220) are along electric conductor assembly (214; 216; 218) length is located such that each heater (212) can be arranged under the situation of not damaging electrical insulator (220) on each bobbin (226).
14. like claim 12 or 13 described methods, wherein three heaters (212) are bonded to support component (224) so that three heaters (212) roughly are evenly spaced apart at support component (224) on every side.
15. the method that arbitrary described heating system heats among utilization such as the claim 1-11, this method comprise the heat from heater (212) is offered a part of subterranean strata.
16. method as claimed in claim 15, wherein subterranean strata comprises hydrocarbon, and this method comprises that also permission heat is passed to the rock stratum so that the pyrolysis in the rock stratum of at least some hydrocarbon.
17. method as claimed in claim 16 also comprises from the formation production fluid.
18. method as claimed in claim 17 also comprises the fluid from formation production is transformed into transport fuel.
CN200680013322.3A 2005-04-22 2006-04-21 Insulation conductor temperature-limiting heater for underground strata heating combined with three-phase y structure Expired - Fee Related CN101163853B (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
US67408105P 2005-04-22 2005-04-22
US60/674,081 2005-04-22
PCT/US2006/015084 WO2006116078A1 (en) 2005-04-22 2006-04-21 Insulated conductor temperature limited heater for subsurface heating coupled in a three-phase wye configuration

Publications (2)

Publication Number Publication Date
CN101163853A CN101163853A (en) 2008-04-16
CN101163853B true CN101163853B (en) 2012-03-21

Family

ID=36655240

Family Applications (12)

Application Number Title Priority Date Filing Date
CN200680013101.6A Expired - Fee Related CN101163855B (en) 2005-04-22 2006-04-21 System for heating subsurface and method for coupling heater in the system
CN200680013312.XA Expired - Fee Related CN101163859B (en) 2005-04-22 2006-04-21 In situ conversion process system using at least two areas with well positioned in subsurface
CN200680013090.1A Expired - Fee Related CN101163854B (en) 2005-04-22 2006-04-21 Temperature limited heater using non-ferromagnetic conductor
CN200680013121.3A Expired - Fee Related CN101163858B (en) 2005-04-22 2006-04-21 In situ conversion system producing hydrocarbon compound from stratum and related method
CN200680013322.3A Expired - Fee Related CN101163853B (en) 2005-04-22 2006-04-21 Insulation conductor temperature-limiting heater for underground strata heating combined with three-phase y structure
CN200680013092.0A Pending CN101163851A (en) 2005-04-22 2006-04-21 Double barrier system for an in situ conversion process
CN200680013103.5A Expired - Fee Related CN101163857B (en) 2005-04-22 2006-04-21 Varying properties along lengths of temperature limited heaters
CN200680013320.4A Expired - Fee Related CN101163856B (en) 2005-04-22 2006-04-21 Grouped exposing metal heater
CN200680013093.5A Expired - Fee Related CN101300401B (en) 2005-04-22 2006-04-21 Methods and systems for producing fluid from an in situ conversion process
CN200680013122.8A Expired - Fee Related CN101163852B (en) 2005-04-22 2006-04-21 Low temperature barriers for in situ processes
CN200680013123.2A Expired - Fee Related CN101163860B (en) 2005-04-22 2006-04-21 Low temperature system for underground barriers
CN200680013130.2A Expired - Fee Related CN101163780B (en) 2005-04-22 2006-04-24 Treatment of gas from an in situ conversion process

Family Applications Before (4)

Application Number Title Priority Date Filing Date
CN200680013101.6A Expired - Fee Related CN101163855B (en) 2005-04-22 2006-04-21 System for heating subsurface and method for coupling heater in the system
CN200680013312.XA Expired - Fee Related CN101163859B (en) 2005-04-22 2006-04-21 In situ conversion process system using at least two areas with well positioned in subsurface
CN200680013090.1A Expired - Fee Related CN101163854B (en) 2005-04-22 2006-04-21 Temperature limited heater using non-ferromagnetic conductor
CN200680013121.3A Expired - Fee Related CN101163858B (en) 2005-04-22 2006-04-21 In situ conversion system producing hydrocarbon compound from stratum and related method

Family Applications After (7)

Application Number Title Priority Date Filing Date
CN200680013092.0A Pending CN101163851A (en) 2005-04-22 2006-04-21 Double barrier system for an in situ conversion process
CN200680013103.5A Expired - Fee Related CN101163857B (en) 2005-04-22 2006-04-21 Varying properties along lengths of temperature limited heaters
CN200680013320.4A Expired - Fee Related CN101163856B (en) 2005-04-22 2006-04-21 Grouped exposing metal heater
CN200680013093.5A Expired - Fee Related CN101300401B (en) 2005-04-22 2006-04-21 Methods and systems for producing fluid from an in situ conversion process
CN200680013122.8A Expired - Fee Related CN101163852B (en) 2005-04-22 2006-04-21 Low temperature barriers for in situ processes
CN200680013123.2A Expired - Fee Related CN101163860B (en) 2005-04-22 2006-04-21 Low temperature system for underground barriers
CN200680013130.2A Expired - Fee Related CN101163780B (en) 2005-04-22 2006-04-24 Treatment of gas from an in situ conversion process

Country Status (14)

Country Link
US (1) US7831133B2 (en)
EP (12) EP1871982B1 (en)
CN (12) CN101163855B (en)
AT (5) ATE463658T1 (en)
AU (13) AU2006239962B8 (en)
CA (12) CA2606210C (en)
DE (5) DE602006007693D1 (en)
EA (12) EA013555B1 (en)
IL (12) IL186206A (en)
IN (1) IN266867B (en)
MA (12) MA29478B1 (en)
NZ (12) NZ562240A (en)
WO (12) WO2006116097A1 (en)
ZA (13) ZA200708022B (en)

Families Citing this family (121)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6880635B2 (en) 2000-04-24 2005-04-19 Shell Oil Company In situ production of synthesis gas from a coal formation, the synthesis gas having a selected H2 to CO ratio
US6991032B2 (en) 2001-04-24 2006-01-31 Shell Oil Company In situ thermal processing of an oil shale formation using a pattern of heat sources
AU2002359315B2 (en) 2001-10-24 2007-11-29 Shell Internationale Research Maatschappij B.V. In situ thermal processing of a hydrocarbon containing formation via backproducing through a heater well
WO2004038174A2 (en) 2002-10-24 2004-05-06 Shell Internationale Research Maatschappij B.V. Staged and/or patterned heating during in situ thermal processing of a hydrocarbon containing formation
NZ567052A (en) * 2003-04-24 2009-11-27 Shell Int Research Thermal process for subsurface formations
NZ550443A (en) 2004-04-23 2010-02-26 Shell Int Research Inhibiting reflux in a heated well of an in situ conversion system
US7024800B2 (en) 2004-07-19 2006-04-11 Earthrenew, Inc. Process and system for drying and heat treating materials
US7694523B2 (en) 2004-07-19 2010-04-13 Earthrenew, Inc. Control system for gas turbine in material treatment unit
US7685737B2 (en) 2004-07-19 2010-03-30 Earthrenew, Inc. Process and system for drying and heat treating materials
US7024796B2 (en) 2004-07-19 2006-04-11 Earthrenew, Inc. Process and apparatus for manufacture of fertilizer products from manure and sewage
AU2006239962B8 (en) 2005-04-22 2010-04-29 Shell Internationale Research Maatschappij B.V. In situ conversion system and method of heating a subsurface formation
US7500528B2 (en) 2005-04-22 2009-03-10 Shell Oil Company Low temperature barrier wellbores formed using water flushing
NZ567257A (en) 2005-10-24 2011-02-25 Shell Int Research Method of cracking a crude product to produce additional crude products
US7610692B2 (en) 2006-01-18 2009-11-03 Earthrenew, Inc. Systems for prevention of HAP emissions and for efficient drying/dehydration processes
RU2008145876A (en) 2006-04-21 2010-05-27 Шелл Интернэшнл Рисерч Маатсхаппий Б.В. (NL) HEATERS WITH RESTRICTION OF TEMPERATURE WHICH USE PHASE TRANSFORMATION OF FERROMAGNETIC MATERIAL
CA2667274A1 (en) 2006-10-20 2008-05-02 Shell Internationale Research Maatschappij B.V. Systems and processes for use in treating subsurface formations
DE102007040606B3 (en) 2007-08-27 2009-02-26 Siemens Ag Method and device for the in situ production of bitumen or heavy oil
AU2008227164B2 (en) 2007-03-22 2014-07-17 Exxonmobil Upstream Research Company Resistive heater for in situ formation heating
EP2142758A1 (en) 2007-04-20 2010-01-13 Shell Internationale Research Maatschappij B.V. Parallel heater system for subsurface formations
US7697806B2 (en) * 2007-05-07 2010-04-13 Verizon Patent And Licensing Inc. Fiber optic cable with detectable ferromagnetic components
WO2008153697A1 (en) 2007-05-25 2008-12-18 Exxonmobil Upstream Research Company A process for producing hydrocarbon fluids combining in situ heating, a power plant and a gas plant
US7866386B2 (en) 2007-10-19 2011-01-11 Shell Oil Company In situ oxidation of subsurface formations
EP2262978A1 (en) 2008-04-18 2010-12-22 Shell Internationale Research Maatschappij B.V. Using mines and tunnels for treating subsurface hydrocarbon containing formations
US8297355B2 (en) * 2008-08-22 2012-10-30 Texaco Inc. Using heat from produced fluids of oil and gas operations to produce energy
DE102008047219A1 (en) 2008-09-15 2010-03-25 Siemens Aktiengesellschaft Process for the extraction of bitumen and / or heavy oil from an underground deposit, associated plant and operating procedures of this plant
US9561066B2 (en) 2008-10-06 2017-02-07 Virender K. Sharma Method and apparatus for tissue ablation
US9561068B2 (en) 2008-10-06 2017-02-07 Virender K. Sharma Method and apparatus for tissue ablation
US20100114082A1 (en) 2008-10-06 2010-05-06 Sharma Virender K Method and Apparatus for the Ablation of Endometrial Tissue
US10695126B2 (en) 2008-10-06 2020-06-30 Santa Anna Tech Llc Catheter with a double balloon structure to generate and apply a heated ablative zone to tissue
US10064697B2 (en) 2008-10-06 2018-09-04 Santa Anna Tech Llc Vapor based ablation system for treating various indications
CN102187054B (en) * 2008-10-13 2014-08-27 国际壳牌研究有限公司 Circulated heated transfer fluid heating of subsurface hydrocarbon formations
US20100200237A1 (en) * 2009-02-12 2010-08-12 Colgate Sam O Methods for controlling temperatures in the environments of gas and oil wells
US8851170B2 (en) 2009-04-10 2014-10-07 Shell Oil Company Heater assisted fluid treatment of a subsurface formation
FR2947587A1 (en) 2009-07-03 2011-01-07 Total Sa PROCESS FOR EXTRACTING HYDROCARBONS BY ELECTROMAGNETIC HEATING OF A SUBTERRANEAN FORMATION IN SITU
CN102031961A (en) * 2009-09-30 2011-04-27 西安威尔罗根能源科技有限公司 Borehole temperature measuring probe
US8257112B2 (en) 2009-10-09 2012-09-04 Shell Oil Company Press-fit coupling joint for joining insulated conductors
US9466896B2 (en) 2009-10-09 2016-10-11 Shell Oil Company Parallelogram coupling joint for coupling insulated conductors
US8356935B2 (en) 2009-10-09 2013-01-22 Shell Oil Company Methods for assessing a temperature in a subsurface formation
US8602103B2 (en) 2009-11-24 2013-12-10 Conocophillips Company Generation of fluid for hydrocarbon recovery
US8863839B2 (en) 2009-12-17 2014-10-21 Exxonmobil Upstream Research Company Enhanced convection for in situ pyrolysis of organic-rich rock formations
US8939207B2 (en) 2010-04-09 2015-01-27 Shell Oil Company Insulated conductor heaters with semiconductor layers
US8502120B2 (en) 2010-04-09 2013-08-06 Shell Oil Company Insulating blocks and methods for installation in insulated conductor heaters
US8875788B2 (en) 2010-04-09 2014-11-04 Shell Oil Company Low temperature inductive heating of subsurface formations
US8631866B2 (en) 2010-04-09 2014-01-21 Shell Oil Company Leak detection in circulated fluid systems for heating subsurface formations
CN102844520B (en) * 2010-04-09 2016-02-03 国际壳牌研究有限公司 The method of two or more heaters is installed in subsurface formations
US9127523B2 (en) 2010-04-09 2015-09-08 Shell Oil Company Barrier methods for use in subsurface hydrocarbon formations
CN102834585B (en) * 2010-04-09 2015-06-17 国际壳牌研究有限公司 Low temperature inductive heating of subsurface formations
US8739874B2 (en) 2010-04-09 2014-06-03 Shell Oil Company Methods for heating with slots in hydrocarbon formations
US8464792B2 (en) 2010-04-27 2013-06-18 American Shale Oil, Llc Conduction convection reflux retorting process
US8408287B2 (en) * 2010-06-03 2013-04-02 Electro-Petroleum, Inc. Electrical jumper for a producing oil well
US8476562B2 (en) 2010-06-04 2013-07-02 Watlow Electric Manufacturing Company Inductive heater humidifier
RU2444617C1 (en) * 2010-08-31 2012-03-10 Открытое акционерное общество "Татнефть" имени В.Д. Шашина Development method of high-viscosity oil deposit using method of steam gravitational action on formation
AT12463U1 (en) * 2010-09-27 2012-05-15 Plansee Se heating conductor
US8857051B2 (en) 2010-10-08 2014-10-14 Shell Oil Company System and method for coupling lead-in conductor to insulated conductor
US8943686B2 (en) 2010-10-08 2015-02-03 Shell Oil Company Compaction of electrical insulation for joining insulated conductors
US8732946B2 (en) 2010-10-08 2014-05-27 Shell Oil Company Mechanical compaction of insulator for insulated conductor splices
CN103314179A (en) * 2010-12-21 2013-09-18 雪佛龙美国公司 System and method for enhancing oil recovery from a subterranean reservoir
RU2473779C2 (en) * 2011-03-21 2013-01-27 Федеральное государственное автономное образовательное учреждение высшего профессионального образования "Северный (Арктический) федеральный университет" (С(А)ФУ) Method of killing fluid fountain from well
US9016370B2 (en) 2011-04-08 2015-04-28 Shell Oil Company Partial solution mining of hydrocarbon containing layers prior to in situ heat treatment
RU2587459C2 (en) 2011-04-08 2016-06-20 Шелл Интернэшнл Рисерч Маатсхаппий Б.В. Systems for joining insulated conductors
EP2520863B1 (en) * 2011-05-05 2016-11-23 General Electric Technology GmbH Method for protecting a gas turbine engine against high dynamical process values and gas turbine engine for conducting said method
US9010428B2 (en) * 2011-09-06 2015-04-21 Baker Hughes Incorporated Swelling acceleration using inductively heated and embedded particles in a subterranean tool
US9080917B2 (en) 2011-10-07 2015-07-14 Shell Oil Company System and methods for using dielectric properties of an insulated conductor in a subsurface formation to assess properties of the insulated conductor
JO3139B1 (en) 2011-10-07 2017-09-20 Shell Int Research Forming insulated conductors using a final reduction step after heat treating
WO2013052561A2 (en) 2011-10-07 2013-04-11 Shell Oil Company Thermal expansion accommodation for circulated fluid systems used to heat subsurface formations
JO3141B1 (en) 2011-10-07 2017-09-20 Shell Int Research Integral splice for insulated conductors
CN102505731A (en) * 2011-10-24 2012-06-20 武汉大学 Groundwater acquisition system under capillary-injection synergic action
US9080441B2 (en) 2011-11-04 2015-07-14 Exxonmobil Upstream Research Company Multiple electrical connections to optimize heating for in situ pyrolysis
CN102434144A (en) * 2011-11-16 2012-05-02 中国石油集团长城钻探工程有限公司 Oil extraction method for u-shaped well for oil field
US8908031B2 (en) * 2011-11-18 2014-12-09 General Electric Company Apparatus and method for measuring moisture content in steam flow
AU2012367826A1 (en) 2012-01-23 2014-08-28 Genie Ip B.V. Heater pattern for in situ thermal processing of a subsurface hydrocarbon containing formation
AU2012367347A1 (en) 2012-01-23 2014-08-28 Genie Ip B.V. Heater pattern for in situ thermal processing of a subsurface hydrocarbon containing formation
US9488027B2 (en) 2012-02-10 2016-11-08 Baker Hughes Incorporated Fiber reinforced polymer matrix nanocomposite downhole member
RU2496979C1 (en) * 2012-05-03 2013-10-27 Открытое акционерное общество "Татнефть" имени В.Д. Шашина Development method of deposit of high-viscosity oil and/or bitumen using method for steam pumping to formation
EP3964151A3 (en) 2013-01-17 2022-03-30 Virender K. Sharma Apparatus for tissue ablation
US9291041B2 (en) * 2013-02-06 2016-03-22 Orbital Atk, Inc. Downhole injector insert apparatus
US9403328B1 (en) * 2013-02-08 2016-08-02 The Boeing Company Magnetic compaction blanket for composite structure curing
US10501348B1 (en) 2013-03-14 2019-12-10 Angel Water, Inc. Water flow triggering of chlorination treatment
RU2527446C1 (en) * 2013-04-15 2014-08-27 Открытое акционерное общество "Татнефть" имени В.Д. Шашина Method of well abandonment
US9382785B2 (en) 2013-06-17 2016-07-05 Baker Hughes Incorporated Shaped memory devices and method for using same in wellbores
CN103321618A (en) * 2013-06-28 2013-09-25 中国地质大学(北京) Oil shale in-situ mining method
CN105518250A (en) * 2013-07-05 2016-04-20 尼克森能源无限责任公司 Solvent addition to improve efficiency of hydrocarbon production
RU2531965C1 (en) * 2013-08-23 2014-10-27 Открытое акционерное общество "Татнефть" имени В.Д. Шашина Method of well abandonment
US9512699B2 (en) 2013-10-22 2016-12-06 Exxonmobil Upstream Research Company Systems and methods for regulating an in situ pyrolysis process
AU2013404088B2 (en) * 2013-10-28 2016-09-22 Halliburton Energy Services, Inc. Downhole communication between wellbores utilizing swellable materials
EP3326716A1 (en) * 2013-10-31 2018-05-30 Reactor Resources, LLC In-situ catalyst sulfiding, passivating and coking methods and systems
US9394772B2 (en) 2013-11-07 2016-07-19 Exxonmobil Upstream Research Company Systems and methods for in situ resistive heating of organic matter in a subterranean formation
CN103628856A (en) * 2013-12-11 2014-03-12 中国地质大学(北京) Water resistance gas production well spacing method for coal-bed gas block highly yielding water
GB2523567B (en) 2014-02-27 2017-12-06 Statoil Petroleum As Producing hydrocarbons from a subsurface formation
CN106460486B (en) * 2014-04-01 2021-10-22 未来E蒸汽有限责任公司 Thermal energy transfer and oil recovery apparatus and method thereof
GB2526123A (en) * 2014-05-14 2015-11-18 Statoil Petroleum As Producing hydrocarbons from a subsurface formation
US20150360322A1 (en) * 2014-06-12 2015-12-17 Siemens Energy, Inc. Laser deposition of iron-based austenitic alloy with flux
RU2569102C1 (en) * 2014-08-12 2015-11-20 Общество с ограниченной ответственностью Научно-инженерный центр "Энергодиагностика" Method for removal of deposits and prevention of their formation in oil well and device for its implementation
US9451792B1 (en) * 2014-09-05 2016-09-27 Atmos Nation, LLC Systems and methods for vaporizing assembly
AU2015350481A1 (en) 2014-11-21 2017-05-25 Exxonmobil Upstream Research Company Method of recovering hydrocarbons within a subsurface formation
RU2728107C2 (en) * 2014-11-25 2020-07-28 Шелл Интернэшнл Рисерч Маатсхаппий Б.В. Pyrolysis to create pressure in oil formations
US20160169451A1 (en) * 2014-12-12 2016-06-16 Fccl Partnership Process and system for delivering steam
CN105043449B (en) * 2015-08-10 2017-12-01 安徽理工大学 Wall temperature, stress and the distribution type fiber-optic of deformation and its method for embedding are freezed in monitoring
US10352818B2 (en) * 2015-08-31 2019-07-16 Halliburton Energy Services, Inc. Monitoring system for cold climate
CN105257269B (en) * 2015-10-26 2017-10-17 中国石油天然气股份有限公司 A kind of steam drive combines oil production method with fireflood
US10125604B2 (en) * 2015-10-27 2018-11-13 Baker Hughes, A Ge Company, Llc Downhole zonal isolation detection system having conductor and method
RU2620820C1 (en) * 2016-02-17 2017-05-30 Общество с ограниченной ответственностью "ЛУКОЙЛ-ПЕРМЬ" Induction well heating device
US11331140B2 (en) 2016-05-19 2022-05-17 Aqua Heart, Inc. Heated vapor ablation systems and methods for treating cardiac conditions
RU2630018C1 (en) * 2016-06-29 2017-09-05 Общество с ограниченной ответчственностью "Геобурсервис", ООО "Геобурсервис" Method for elimination, prevention of sediments formation and intensification of oil production in oil and gas wells and device for its implementation
US11486243B2 (en) * 2016-08-04 2022-11-01 Baker Hughes Esp, Inc. ESP gas slug avoidance system
RU2632791C1 (en) * 2016-11-02 2017-10-09 Владимир Иванович Савичев Method for stimulation of wells by injecting gas compositions
CN107289997B (en) * 2017-05-05 2019-08-13 济南轨道交通集团有限公司 A kind of Karst-fissure water detection system and method
US10626709B2 (en) * 2017-06-08 2020-04-21 Saudi Arabian Oil Company Steam driven submersible pump
CN107558950A (en) * 2017-09-13 2018-01-09 吉林大学 Orientation blocking method for the closing of oil shale underground in situ production zone
EP3801324A4 (en) 2018-06-01 2022-03-30 Santa Anna Tech LLC Multi-stage vapor-based ablation treatment methods and vapor generation and delivery systems
US10927645B2 (en) * 2018-08-20 2021-02-23 Baker Hughes, A Ge Company, Llc Heater cable with injectable fiber optics
CN109379792A (en) * 2018-11-12 2019-02-22 山东华宁电伴热科技有限公司 A kind of heating cable for oil well and heating oil well method
CN109396168B (en) * 2018-12-01 2023-12-26 中节能城市节能研究院有限公司 Combined heat exchanger for in-situ thermal remediation of polluted soil and soil thermal remediation system
CN109399879B (en) * 2018-12-14 2023-10-20 江苏筑港建设集团有限公司 Curing method of dredger fill mud quilt
FR3093588B1 (en) * 2019-03-07 2021-02-26 Socomec Sa ENERGY RECOVERY DEVICE ON AT LEAST ONE POWER CONDUCTOR AND MANUFACTURING PROCESS OF SAID RECOVERY DEVICE
US11708757B1 (en) * 2019-05-14 2023-07-25 Fortress Downhole Tools, Llc Method and apparatus for testing setting tools and other assemblies used to set downhole plugs and other objects in wellbores
US11136514B2 (en) * 2019-06-07 2021-10-05 Uop Llc Process and apparatus for recycling hydrogen to hydroprocess biorenewable feed
GB2605722A (en) * 2019-12-11 2022-10-12 Aker Solutions As Skin-effect heating cable
DE102020208178A1 (en) * 2020-06-30 2021-12-30 Robert Bosch Gesellschaft mit beschränkter Haftung Method for heating a fuel cell system, fuel cell system, use of an electrical heating element
CN112485119B (en) * 2020-11-09 2023-01-31 临沂矿业集团有限责任公司 Mining hoisting winch steel wire rope static tension test vehicle
EP4113768A1 (en) * 2021-07-02 2023-01-04 Nexans Dry-mate wet-design branch joint and method for realizing a subsea distribution of electric power for wet cables

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN85109007A (en) * 1985-12-09 1987-06-24 国际壳牌研究有限公司 Method and apparatus for installation of electric heater
CN1236858A (en) * 1998-03-06 1999-12-01 国际壳牌研究有限公司 Electrical heater
CN1430696A (en) * 2000-04-24 2003-07-16 国际壳牌研究有限公司 Heating system and method

Family Cites Families (268)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2732195A (en) 1956-01-24 Ljungstrom
CA899987A (en) 1972-05-09 Chisso Corporation Method for controlling heat generation locally in a heat-generating pipe utilizing skin effect current
SE126674C1 (en) 1949-01-01
US48994A (en) 1865-07-25 Improvement in devices for oil-wells
SE123136C1 (en) 1948-01-01
US345586A (en) * 1886-07-13 Oil from wells
SE123138C1 (en) 1948-01-01
US94813A (en) 1869-09-14 Improvement in torpedoes for oil-wells
US326439A (en) 1885-09-15 Protecting wells
US2734579A (en) 1956-02-14 Production from bituminous sands
US438461A (en) * 1890-10-14 Half to william j
US760304A (en) 1903-10-24 1904-05-17 Frank S Gilbert Heater for oil-wells.
US1342741A (en) 1918-01-17 1920-06-08 David T Day Process for extracting oils and hydrocarbon material from shale and similar bituminous rocks
US1269747A (en) 1918-04-06 1918-06-18 Lebbeus H Rogers Method of and apparatus for treating oil-shale.
GB156396A (en) 1919-12-10 1921-01-13 Wilson Woods Hoover An improved method of treating shale and recovering oil therefrom
US1457479A (en) 1920-01-12 1923-06-05 Edson R Wolcott Method of increasing the yield of oil wells
US1510655A (en) 1922-11-21 1924-10-07 Clark Cornelius Process of subterranean distillation of volatile mineral substances
US1634236A (en) 1925-03-10 1927-06-28 Standard Dev Co Method of and apparatus for recovering oil
US1646599A (en) * 1925-04-30 1927-10-25 George A Schaefer Apparatus for removing fluid from wells
US1666488A (en) 1927-02-05 1928-04-17 Crawshaw Richard Apparatus for extracting oil from shale
US1681523A (en) 1927-03-26 1928-08-21 Patrick V Downey Apparatus for heating oil wells
US1913395A (en) 1929-11-14 1933-06-13 Lewis C Karrick Underground gasification of carbonaceous material-bearing substances
US2244255A (en) * 1939-01-18 1941-06-03 Electrical Treating Company Well clearing system
US2244256A (en) 1939-12-16 1941-06-03 Electrical Treating Company Apparatus for clearing wells
US2319702A (en) 1941-04-04 1943-05-18 Socony Vacuum Oil Co Inc Method and apparatus for producing oil wells
US2365591A (en) 1942-08-15 1944-12-19 Ranney Leo Method for producing oil from viscous deposits
US2423674A (en) 1942-08-24 1947-07-08 Johnson & Co A Process of catalytic cracking of petroleum hydrocarbons
US2390770A (en) * 1942-10-10 1945-12-11 Sun Oil Co Method of producing petroleum
US2484063A (en) 1944-08-19 1949-10-11 Thermactor Corp Electric heater for subsurface materials
US2472445A (en) 1945-02-02 1949-06-07 Thermactor Company Apparatus for treating oil and gas bearing strata
US2481051A (en) 1945-12-15 1949-09-06 Texaco Development Corp Process and apparatus for the recovery of volatilizable constituents from underground carbonaceous formations
US2444755A (en) 1946-01-04 1948-07-06 Ralph M Steffen Apparatus for oil sand heating
US2634961A (en) 1946-01-07 1953-04-14 Svensk Skifferolje Aktiebolage Method of electrothermal production of shale oil
US2466945A (en) 1946-02-21 1949-04-12 In Situ Gases Inc Generation of synthesis gas
US2497868A (en) 1946-10-10 1950-02-21 Dalin David Underground exploitation of fuel deposits
US2939689A (en) 1947-06-24 1960-06-07 Svenska Skifferolje Ab Electrical heater for treating oilshale and the like
US2786660A (en) 1948-01-05 1957-03-26 Phillips Petroleum Co Apparatus for gasifying coal
US2548360A (en) 1948-03-29 1951-04-10 Stanley A Germain Electric oil well heater
US2685930A (en) 1948-08-12 1954-08-10 Union Oil Co Oil well production process
US2757738A (en) * 1948-09-20 1956-08-07 Union Oil Co Radiation heating
US2630307A (en) 1948-12-09 1953-03-03 Carbonic Products Inc Method of recovering oil from oil shale
US2595979A (en) 1949-01-25 1952-05-06 Texas Co Underground liquefaction of coal
US2642943A (en) 1949-05-20 1953-06-23 Sinclair Oil & Gas Co Oil recovery process
US2593477A (en) 1949-06-10 1952-04-22 Us Interior Process of underground gasification of coal
US2670802A (en) 1949-12-16 1954-03-02 Thermactor Company Reviving or increasing the production of clogged or congested oil wells
US2714930A (en) 1950-12-08 1955-08-09 Union Oil Co Apparatus for preventing paraffin deposition
US2695163A (en) 1950-12-09 1954-11-23 Stanolind Oil & Gas Co Method for gasification of subterranean carbonaceous deposits
US2630306A (en) 1952-01-03 1953-03-03 Socony Vacuum Oil Co Inc Subterranean retorting of shales
US2757739A (en) 1952-01-07 1956-08-07 Parelex Corp Heating apparatus
US2777679A (en) 1952-03-07 1957-01-15 Svenska Skifferolje Ab Recovering sub-surface bituminous deposits by creating a frozen barrier and heating in situ
US2780450A (en) 1952-03-07 1957-02-05 Svenska Skifferolje Ab Method of recovering oil and gases from non-consolidated bituminous geological formations by a heating treatment in situ
US2789805A (en) 1952-05-27 1957-04-23 Svenska Skifferolje Ab Device for recovering fuel from subterraneous fuel-carrying deposits by heating in their natural location using a chain heat transfer member
GB774283A (en) * 1952-09-15 1957-05-08 Ruhrchemie Ag Process for the combined purification and methanisation of gas mixtures containing oxides of carbon and hydrogen
US2780449A (en) 1952-12-26 1957-02-05 Sinclair Oil & Gas Co Thermal process for in-situ decomposition of oil shale
US2825408A (en) * 1953-03-09 1958-03-04 Sinclair Oil & Gas Company Oil recovery by subsurface thermal processing
US2771954A (en) 1953-04-29 1956-11-27 Exxon Research Engineering Co Treatment of petroleum production wells
US2703621A (en) 1953-05-04 1955-03-08 George W Ford Oil well bottom hole flow increasing unit
US2743906A (en) * 1953-05-08 1956-05-01 William E Coyle Hydraulic underreamer
US2803305A (en) * 1953-05-14 1957-08-20 Pan American Petroleum Corp Oil recovery by underground combustion
US2914309A (en) 1953-05-25 1959-11-24 Svenska Skifferolje Ab Oil and gas recovery from tar sands
US2902270A (en) 1953-07-17 1959-09-01 Svenska Skifferolje Ab Method of and means in heating of subsurface fuel-containing deposits "in situ"
US2890754A (en) 1953-10-30 1959-06-16 Svenska Skifferolje Ab Apparatus for recovering combustible substances from subterraneous deposits in situ
US2890755A (en) 1953-12-19 1959-06-16 Svenska Skifferolje Ab Apparatus for recovering combustible substances from subterraneous deposits in situ
US2841375A (en) 1954-03-03 1958-07-01 Svenska Skifferolje Ab Method for in-situ utilization of fuels by combustion
US2794504A (en) * 1954-05-10 1957-06-04 Union Oil Co Well heater
US2793696A (en) 1954-07-22 1957-05-28 Pan American Petroleum Corp Oil recovery by underground combustion
US2923535A (en) 1955-02-11 1960-02-02 Svenska Skifferolje Ab Situ recovery from carbonaceous deposits
US2801089A (en) * 1955-03-14 1957-07-30 California Research Corp Underground shale retorting process
US2862558A (en) 1955-12-28 1958-12-02 Phillips Petroleum Co Recovering oils from formations
US2819761A (en) * 1956-01-19 1958-01-14 Continental Oil Co Process of removing viscous oil from a well bore
US2857002A (en) * 1956-03-19 1958-10-21 Texas Co Recovery of viscous crude oil
US2906340A (en) 1956-04-05 1959-09-29 Texaco Inc Method of treating a petroleum producing formation
US2991046A (en) 1956-04-16 1961-07-04 Parsons Lional Ashley Combined winch and bollard device
US2997105A (en) 1956-10-08 1961-08-22 Pan American Petroleum Corp Burner apparatus
US2932352A (en) 1956-10-25 1960-04-12 Union Oil Co Liquid filled well heater
US2804149A (en) 1956-12-12 1957-08-27 John R Donaldson Oil well heater and reviver
US2942223A (en) 1957-08-09 1960-06-21 Gen Electric Electrical resistance heater
US2906337A (en) 1957-08-16 1959-09-29 Pure Oil Co Method of recovering bitumen
US2954826A (en) 1957-12-02 1960-10-04 William E Sievers Heated well production string
US2994376A (en) * 1957-12-27 1961-08-01 Phillips Petroleum Co In situ combustion process
US3051235A (en) 1958-02-24 1962-08-28 Jersey Prod Res Co Recovery of petroleum crude oil, by in situ combustion and in situ hydrogenation
US2911047A (en) * 1958-03-11 1959-11-03 John C Henderson Apparatus for extracting naturally occurring difficultly flowable petroleum oil from a naturally located subterranean body
US2958519A (en) * 1958-06-23 1960-11-01 Phillips Petroleum Co In situ combustion process
US2974937A (en) * 1958-11-03 1961-03-14 Jersey Prod Res Co Petroleum recovery from carbonaceous formations
US2998457A (en) * 1958-11-19 1961-08-29 Ashland Oil Inc Production of phenols
US2970826A (en) * 1958-11-21 1961-02-07 Texaco Inc Recovery of oil from oil shale
US3097690A (en) 1958-12-24 1963-07-16 Gulf Research Development Co Process for heating a subsurface formation
US2969226A (en) * 1959-01-19 1961-01-24 Pyrochem Corp Pendant parting petro pyrolysis process
US3150715A (en) 1959-09-30 1964-09-29 Shell Oil Co Oil recovery by in situ combustion with water injection
US3170519A (en) * 1960-05-11 1965-02-23 Gordon L Allot Oil well microwave tools
US3058730A (en) 1960-06-03 1962-10-16 Fmc Corp Method of forming underground communication between boreholes
US3138203A (en) 1961-03-06 1964-06-23 Jersey Prod Res Co Method of underground burning
US3057404A (en) 1961-09-29 1962-10-09 Socony Mobil Oil Co Inc Method and system for producing oil tenaciously held in porous formations
US3194315A (en) * 1962-06-26 1965-07-13 Charles D Golson Apparatus for isolating zones in wells
US3272261A (en) 1963-12-13 1966-09-13 Gulf Research Development Co Process for recovery of oil
US3332480A (en) 1965-03-04 1967-07-25 Pan American Petroleum Corp Recovery of hydrocarbons by thermal methods
US3358756A (en) 1965-03-12 1967-12-19 Shell Oil Co Method for in situ recovery of solid or semi-solid petroleum deposits
US3262741A (en) 1965-04-01 1966-07-26 Pittsburgh Plate Glass Co Solution mining of potassium chloride
US3278234A (en) 1965-05-17 1966-10-11 Pittsburgh Plate Glass Co Solution mining of potassium chloride
US3362751A (en) 1966-02-28 1968-01-09 Tinlin William Method and system for recovering shale oil and gas
DE1615192B1 (en) 1966-04-01 1970-08-20 Chisso Corp Inductively heated heating pipe
US3410796A (en) 1966-04-04 1968-11-12 Gas Processors Inc Process for treatment of saline waters
US3372754A (en) 1966-05-31 1968-03-12 Mobil Oil Corp Well assembly for heating a subterranean formation
US3399623A (en) 1966-07-14 1968-09-03 James R. Creed Apparatus for and method of producing viscid oil
NL153755C (en) 1966-10-20 1977-11-15 Stichting Reactor Centrum METHOD FOR MANUFACTURING AN ELECTRIC HEATING ELEMENT, AS WELL AS HEATING ELEMENT MANUFACTURED USING THIS METHOD.
US3465819A (en) 1967-02-13 1969-09-09 American Oil Shale Corp Use of nuclear detonations in producing hydrocarbons from an underground formation
NL6803827A (en) 1967-03-22 1968-09-23
US3542276A (en) * 1967-11-13 1970-11-24 Ideal Ind Open type explosion connector and method
US3485300A (en) 1967-12-20 1969-12-23 Phillips Petroleum Co Method and apparatus for defoaming crude oil down hole
US3578080A (en) 1968-06-10 1971-05-11 Shell Oil Co Method of producing shale oil from an oil shale formation
US3537528A (en) 1968-10-14 1970-11-03 Shell Oil Co Method for producing shale oil from an exfoliated oil shale formation
US3593789A (en) 1968-10-18 1971-07-20 Shell Oil Co Method for producing shale oil from an oil shale formation
US3565171A (en) 1968-10-23 1971-02-23 Shell Oil Co Method for producing shale oil from a subterranean oil shale formation
US3554285A (en) 1968-10-24 1971-01-12 Phillips Petroleum Co Production and upgrading of heavy viscous oils
US3629551A (en) 1968-10-29 1971-12-21 Chisso Corp Controlling heat generation locally in a heat-generating pipe utilizing skin-effect current
US3513249A (en) * 1968-12-24 1970-05-19 Ideal Ind Explosion connector with improved insulating means
US3614986A (en) * 1969-03-03 1971-10-26 Electrothermic Co Method for injecting heated fluids into mineral bearing formations
US3542131A (en) 1969-04-01 1970-11-24 Mobil Oil Corp Method of recovering hydrocarbons from oil shale
US3547192A (en) 1969-04-04 1970-12-15 Shell Oil Co Method of metal coating and electrically heating a subterranean earth formation
US3529075A (en) * 1969-05-21 1970-09-15 Ideal Ind Explosion connector with ignition arrangement
US3572838A (en) 1969-07-07 1971-03-30 Shell Oil Co Recovery of aluminum compounds and oil from oil shale formations
US3614387A (en) 1969-09-22 1971-10-19 Watlow Electric Mfg Co Electrical heater with an internal thermocouple
US3679812A (en) 1970-11-13 1972-07-25 Schlumberger Technology Corp Electrical suspension cable for well tools
US3893918A (en) 1971-11-22 1975-07-08 Engineering Specialties Inc Method for separating material leaving a well
US3757860A (en) 1972-08-07 1973-09-11 Atlantic Richfield Co Well heating
US3761599A (en) 1972-09-05 1973-09-25 Gen Electric Means for reducing eddy current heating of a tank in electric apparatus
US3794113A (en) 1972-11-13 1974-02-26 Mobil Oil Corp Combination in situ combustion displacement and steam stimulation of producing wells
US4199025A (en) 1974-04-19 1980-04-22 Electroflood Company Method and apparatus for tertiary recovery of oil
US4037655A (en) 1974-04-19 1977-07-26 Electroflood Company Method for secondary recovery of oil
US3894769A (en) 1974-06-06 1975-07-15 Shell Oil Co Recovering oil from a subterranean carbonaceous formation
US4029360A (en) 1974-07-26 1977-06-14 Occidental Oil Shale, Inc. Method of recovering oil and water from in situ oil shale retort flue gas
US3933447A (en) 1974-11-08 1976-01-20 The United States Of America As Represented By The United States Energy Research And Development Administration Underground gasification of coal
US3950029A (en) 1975-06-12 1976-04-13 Mobil Oil Corporation In situ retorting of oil shale
US4199024A (en) 1975-08-07 1980-04-22 World Energy Systems Multistage gas generator
US4037658A (en) 1975-10-30 1977-07-26 Chevron Research Company Method of recovering viscous petroleum from an underground formation
US4018279A (en) 1975-11-12 1977-04-19 Reynolds Merrill J In situ coal combustion heat recovery method
US4017319A (en) 1976-01-06 1977-04-12 General Electric Company Si3 N4 formed by nitridation of sintered silicon compact containing boron
US4487257A (en) 1976-06-17 1984-12-11 Raytheon Company Apparatus and method for production of organic products from kerogen
US4083604A (en) 1976-11-15 1978-04-11 Trw Inc. Thermomechanical fracture for recovery system in oil shale deposits
US4169506A (en) 1977-07-15 1979-10-02 Standard Oil Company (Indiana) In situ retorting of oil shale and energy recovery
US4119349A (en) 1977-10-25 1978-10-10 Gulf Oil Corporation Method and apparatus for recovery of fluids produced in in-situ retorting of oil shale
US4228853A (en) 1978-06-21 1980-10-21 Harvey A Herbert Petroleum production method
US4446917A (en) 1978-10-04 1984-05-08 Todd John C Method and apparatus for producing viscous or waxy crude oils
US4311340A (en) 1978-11-27 1982-01-19 Lyons William C Uranium leeching process and insitu mining
JPS5576586A (en) 1978-12-01 1980-06-09 Tokyo Shibaura Electric Co Heater
US4457365A (en) 1978-12-07 1984-07-03 Raytheon Company In situ radio frequency selective heating system
US4232902A (en) 1979-02-09 1980-11-11 Ppg Industries, Inc. Solution mining water soluble salts at high temperatures
US4289354A (en) 1979-02-23 1981-09-15 Edwin G. Higgins, Jr. Borehole mining of solid mineral resources
US4290650A (en) 1979-08-03 1981-09-22 Ppg Industries Canada Ltd. Subterranean cavity chimney development for connecting solution mined cavities
CA1168283A (en) 1980-04-14 1984-05-29 Hiroshi Teratani Electrode device for electrically heating underground deposits of hydrocarbons
CA1165361A (en) 1980-06-03 1984-04-10 Toshiyuki Kobayashi Electrode unit for electrically heating underground hydrocarbon deposits
US4401099A (en) 1980-07-11 1983-08-30 W.B. Combustion, Inc. Single-ended recuperative radiant tube assembly and method
US4385661A (en) 1981-01-07 1983-05-31 The United States Of America As Represented By The United States Department Of Energy Downhole steam generator with improved preheating, combustion and protection features
US4382469A (en) 1981-03-10 1983-05-10 Electro-Petroleum, Inc. Method of in situ gasification
GB2110231B (en) * 1981-03-13 1984-11-14 Jgc Corp Process for converting solid wastes to gases for use as a town gas
US4384614A (en) * 1981-05-11 1983-05-24 Justheim Pertroleum Company Method of retorting oil shale by velocity flow of super-heated air
US4401162A (en) 1981-10-13 1983-08-30 Synfuel (An Indiana Limited Partnership) In situ oil shale process
US4549073A (en) 1981-11-06 1985-10-22 Oximetrix, Inc. Current controller for resistive heating element
US4418752A (en) 1982-01-07 1983-12-06 Conoco Inc. Thermal oil recovery with solvent recirculation
US4441985A (en) 1982-03-08 1984-04-10 Exxon Research And Engineering Co. Process for supplying the heat requirement of a retort for recovering oil from solids by partial indirect heating of in situ combustion gases, and combustion air, without the use of supplemental fuel
CA1196594A (en) 1982-04-08 1985-11-12 Guy Savard Recovery of oil from tar sands
US4460044A (en) 1982-08-31 1984-07-17 Chevron Research Company Advancing heated annulus steam drive
US4485868A (en) 1982-09-29 1984-12-04 Iit Research Institute Method for recovery of viscous hydrocarbons by electromagnetic heating in situ
US4498531A (en) 1982-10-01 1985-02-12 Rockwell International Corporation Emission controller for indirect fired downhole steam generators
US4609041A (en) 1983-02-10 1986-09-02 Magda Richard M Well hot oil system
US4886118A (en) * 1983-03-21 1989-12-12 Shell Oil Company Conductively heating a subterranean oil shale to create permeability and subsequently produce oil
US4545435A (en) * 1983-04-29 1985-10-08 Iit Research Institute Conduction heating of hydrocarbonaceous formations
EP0130671A3 (en) 1983-05-26 1986-12-17 Metcal Inc. Multiple temperature autoregulating heater
US4538682A (en) 1983-09-08 1985-09-03 Mcmanus James W Method and apparatus for removing oil well paraffin
US4572229A (en) 1984-02-02 1986-02-25 Thomas D. Mueller Variable proportioner
US4637464A (en) * 1984-03-22 1987-01-20 Amoco Corporation In situ retorting of oil shale with pulsed water purge
US4570715A (en) * 1984-04-06 1986-02-18 Shell Oil Company Formation-tailored method and apparatus for uniformly heating long subterranean intervals at high temperature
US4577691A (en) 1984-09-10 1986-03-25 Texaco Inc. Method and apparatus for producing viscous hydrocarbons from a subterranean formation
JPS61104582A (en) 1984-10-25 1986-05-22 株式会社デンソー Sheathed heater
FR2575463B1 (en) * 1984-12-28 1987-03-20 Gaz De France PROCESS FOR PRODUCING METHANE USING A THORORESISTANT CATALYST AND CATALYST FOR CARRYING OUT SAID METHOD
US4662437A (en) * 1985-11-14 1987-05-05 Atlantic Richfield Company Electrically stimulated well production system with flexible tubing conductor
CA1253555A (en) 1985-11-21 1989-05-02 Cornelis F.H. Van Egmond Heating rate variant elongated electrical resistance heater
CN1006920B (en) * 1985-12-09 1990-02-21 国际壳牌研究有限公司 Method for temp. measuring of small-sized well
US4716960A (en) 1986-07-14 1988-01-05 Production Technologies International, Inc. Method and system for introducing electric current into a well
CA1288043C (en) 1986-12-15 1991-08-27 Peter Van Meurs Conductively heating a subterranean oil shale to create permeabilityand subsequently produce oil
US4793409A (en) 1987-06-18 1988-12-27 Ors Development Corporation Method and apparatus for forming an insulated oil well casing
US4852648A (en) 1987-12-04 1989-08-01 Ava International Corporation Well installation in which electrical current is supplied for a source at the wellhead to an electrically responsive device located a substantial distance below the wellhead
US4974425A (en) 1988-12-08 1990-12-04 Concept Rkk, Limited Closed cryogenic barrier for containment of hazardous material migration in the earth
US4860544A (en) 1988-12-08 1989-08-29 Concept R.K.K. Limited Closed cryogenic barrier for containment of hazardous material migration in the earth
US5152341A (en) 1990-03-09 1992-10-06 Raymond S. Kasevich Electromagnetic method and apparatus for the decontamination of hazardous material-containing volumes
CA2015460C (en) 1990-04-26 1993-12-14 Kenneth Edwin Kisman Process for confining steam injected into a heavy oil reservoir
US5050601A (en) 1990-05-29 1991-09-24 Joel Kupersmith Cardiac defibrillator electrode arrangement
US5042579A (en) 1990-08-23 1991-08-27 Shell Oil Company Method and apparatus for producing tar sand deposits containing conductive layers
US5066852A (en) 1990-09-17 1991-11-19 Teledyne Ind. Inc. Thermoplastic end seal for electric heating elements
US5065818A (en) 1991-01-07 1991-11-19 Shell Oil Company Subterranean heaters
US5732771A (en) 1991-02-06 1998-03-31 Moore; Boyd B. Protective sheath for protecting and separating a plurality of insulated cable conductors for an underground well
CN2095278U (en) * 1991-06-19 1992-02-05 中国石油天然气总公司辽河设计院 Electric heater for oil well
US5133406A (en) 1991-07-05 1992-07-28 Amoco Corporation Generating oxygen-depleted air useful for increasing methane production
US5420402A (en) 1992-02-05 1995-05-30 Iit Research Institute Methods and apparatus to confine earth currents for recovery of subsurface volatiles and semi-volatiles
CN2183444Y (en) * 1993-10-19 1994-11-23 刘犹斌 Electromagnetic heating device for deep-well petroleum
US5507149A (en) 1994-12-15 1996-04-16 Dash; J. Gregory Nonporous liquid impermeable cryogenic barrier
EA000057B1 (en) * 1995-04-07 1998-04-30 Шелл Интернэшнл Рисерч Маатсхаппий Б.В. Oil production well and assembly of such wells
US5730550A (en) * 1995-08-15 1998-03-24 Board Of Trustees Operating Michigan State University Method for placement of a permeable remediation zone in situ
US5759022A (en) 1995-10-16 1998-06-02 Gas Research Institute Method and system for reducing NOx and fuel emissions in a furnace
US5619611A (en) 1995-12-12 1997-04-08 Tub Tauch-Und Baggertechnik Gmbh Device for removing downhole deposits utilizing tubular housing and passing electric current through fluid heating medium contained therein
GB9526120D0 (en) * 1995-12-21 1996-02-21 Raychem Sa Nv Electrical connector
CA2177726C (en) 1996-05-29 2000-06-27 Theodore Wildi Low-voltage and low flux density heating system
US5782301A (en) 1996-10-09 1998-07-21 Baker Hughes Incorporated Oil well heater cable
US6039121A (en) 1997-02-20 2000-03-21 Rangewest Technologies Ltd. Enhanced lift method and apparatus for the production of hydrocarbons
US6540018B1 (en) 1998-03-06 2003-04-01 Shell Oil Company Method and apparatus for heating a wellbore
US6248230B1 (en) * 1998-06-25 2001-06-19 Sk Corporation Method for manufacturing cleaner fuels
US6130398A (en) 1998-07-09 2000-10-10 Illinois Tool Works Inc. Plasma cutter for auxiliary power output of a power source
NO984235L (en) 1998-09-14 2000-03-15 Cit Alcatel Heating system for metal pipes for crude oil transport
AU761606B2 (en) * 1998-09-25 2003-06-05 Errol A. Sonnier System, apparatus, and method for installing control lines in a well
US6609761B1 (en) 1999-01-08 2003-08-26 American Soda, Llp Sodium carbonate and sodium bicarbonate production from nahcolitic oil shale
JP2000340350A (en) 1999-05-28 2000-12-08 Kyocera Corp Silicon nitride ceramic heater and its manufacture
US6257334B1 (en) 1999-07-22 2001-07-10 Alberta Oil Sands Technology And Research Authority Steam-assisted gravity drainage heavy oil recovery process
US6633236B2 (en) 2000-01-24 2003-10-14 Shell Oil Company Permanent downhole, wireless, two-way telemetry backbone using redundant repeaters
US7259688B2 (en) 2000-01-24 2007-08-21 Shell Oil Company Wireless reservoir production control
US20020036085A1 (en) 2000-01-24 2002-03-28 Bass Ronald Marshall Toroidal choke inductor for wireless communication and control
MY128294A (en) 2000-03-02 2007-01-31 Shell Int Research Use of downhole high pressure gas in a gas-lift well
AU2001243413B2 (en) 2000-03-02 2004-10-07 Shell Internationale Research Maatschappij B.V. Controlled downhole chemical injection
US7170424B2 (en) 2000-03-02 2007-01-30 Shell Oil Company Oil well casting electrical power pick-off points
US6632047B2 (en) * 2000-04-14 2003-10-14 Board Of Regents, The University Of Texas System Heater element for use in an in situ thermal desorption soil remediation system
US6918444B2 (en) 2000-04-19 2005-07-19 Exxonmobil Upstream Research Company Method for production of hydrocarbons from organic-rich rock
US7011154B2 (en) 2000-04-24 2006-03-14 Shell Oil Company In situ recovery from a kerogen and liquid hydrocarbon containing formation
US6880635B2 (en) 2000-04-24 2005-04-19 Shell Oil Company In situ production of synthesis gas from a coal formation, the synthesis gas having a selected H2 to CO ratio
US20030066642A1 (en) 2000-04-24 2003-04-10 Wellington Scott Lee In situ thermal processing of a coal formation producing a mixture with oxygenated hydrocarbons
US20030085034A1 (en) 2000-04-24 2003-05-08 Wellington Scott Lee In situ thermal processing of a coal formation to produce pyrolsis products
US7096953B2 (en) 2000-04-24 2006-08-29 Shell Oil Company In situ thermal processing of a coal formation using a movable heating element
WO2002086283A1 (en) * 2001-04-24 2002-10-31 Shell Internationale Research Maatschappij B.V. In-situ combustion for oil recovery
US20030075318A1 (en) 2000-04-24 2003-04-24 Keedy Charles Robert In situ thermal processing of a coal formation using substantially parallel formed wellbores
GB2383633A (en) 2000-06-29 2003-07-02 Paulo S Tubel Method and system for monitoring smart structures utilizing distributed optical sensors
US6585046B2 (en) 2000-08-28 2003-07-01 Baker Hughes Incorporated Live well heater cable
US20020112987A1 (en) 2000-12-15 2002-08-22 Zhiguo Hou Slurry hydroprocessing for heavy oil upgrading using supported slurry catalysts
US20020112890A1 (en) 2001-01-22 2002-08-22 Wentworth Steven W. Conduit pulling apparatus and method for use in horizontal drilling
US20020153141A1 (en) 2001-04-19 2002-10-24 Hartman Michael G. Method for pumping fluids
US6948562B2 (en) 2001-04-24 2005-09-27 Shell Oil Company Production of a blending agent using an in situ thermal process in a relatively permeable formation
US6991032B2 (en) 2001-04-24 2006-01-31 Shell Oil Company In situ thermal processing of an oil shale formation using a pattern of heat sources
US6782947B2 (en) 2001-04-24 2004-08-31 Shell Oil Company In situ thermal processing of a relatively impermeable formation to increase permeability of the formation
AU2002304692C1 (en) 2001-04-24 2009-05-28 Shell Internationale Research Maatschappij B.V. Method for in situ recovery from a tar sands formation and a blending agent produced by such a method
US20030029617A1 (en) 2001-08-09 2003-02-13 Anadarko Petroleum Company Apparatus, method and system for single well solution-mining
US7104319B2 (en) 2001-10-24 2006-09-12 Shell Oil Company In situ thermal processing of a heavy oil diatomite formation
US7077199B2 (en) 2001-10-24 2006-07-18 Shell Oil Company In situ thermal processing of an oil reservoir formation
US6969123B2 (en) 2001-10-24 2005-11-29 Shell Oil Company Upgrading and mining of coal
AU2002359315B2 (en) 2001-10-24 2007-11-29 Shell Internationale Research Maatschappij B.V. In situ thermal processing of a hydrocarbon containing formation via backproducing through a heater well
US7165615B2 (en) 2001-10-24 2007-01-23 Shell Oil Company In situ recovery from a hydrocarbon containing formation using conductor-in-conduit heat sources with an electrically conductive material in the overburden
US7090013B2 (en) 2001-10-24 2006-08-15 Shell Oil Company In situ thermal processing of a hydrocarbon containing formation to produce heated fluids
ATE402294T1 (en) 2001-10-24 2008-08-15 Shell Int Research ICING OF SOILS AS AN PRELIMINARY MEASURE FOR THERMAL TREATMENT
US6679326B2 (en) 2002-01-15 2004-01-20 Bohdan Zakiewicz Pro-ecological mining system
US6973973B2 (en) * 2002-01-22 2005-12-13 Weatherford/Lamb, Inc. Gas operated pump for hydrocarbon wells
US6958195B2 (en) 2002-02-19 2005-10-25 Utc Fuel Cells, Llc Steam generator for a PEM fuel cell power plant
US20040011950A1 (en) * 2002-05-31 2004-01-22 Harkins Gary O. Parameter sensing apparatus and method for subterranean wells
CA2499760C (en) 2002-08-21 2010-02-02 Presssol Ltd. Reverse circulation directional and horizontal drilling using concentric coil tubing
WO2004038174A2 (en) 2002-10-24 2004-05-06 Shell Internationale Research Maatschappij B.V. Staged and/or patterned heating during in situ thermal processing of a hydrocarbon containing formation
US7048051B2 (en) 2003-02-03 2006-05-23 Gen Syn Fuels Recovery of products from oil shale
US6796139B2 (en) 2003-02-27 2004-09-28 Layne Christensen Company Method and apparatus for artificial ground freezing
NZ567052A (en) 2003-04-24 2009-11-27 Shell Int Research Thermal process for subsurface formations
RU2349745C2 (en) 2003-06-24 2009-03-20 Эксонмобил Апстрим Рисерч Компани Method of processing underground formation for conversion of organic substance into extracted hydrocarbons (versions)
US7147057B2 (en) 2003-10-06 2006-12-12 Halliburton Energy Services, Inc. Loop systems and methods of using the same for conveying and distributing thermal energy into a wellbore
US7337841B2 (en) 2004-03-24 2008-03-04 Halliburton Energy Services, Inc. Casing comprising stress-absorbing materials and associated methods of use
NZ550443A (en) 2004-04-23 2010-02-26 Shell Int Research Inhibiting reflux in a heated well of an in situ conversion system
US7500528B2 (en) 2005-04-22 2009-03-10 Shell Oil Company Low temperature barrier wellbores formed using water flushing
AU2006239962B8 (en) 2005-04-22 2010-04-29 Shell Internationale Research Maatschappij B.V. In situ conversion system and method of heating a subsurface formation
NZ567257A (en) 2005-10-24 2011-02-25 Shell Int Research Method of cracking a crude product to produce additional crude products
US7124584B1 (en) 2005-10-31 2006-10-24 General Electric Company System and method for heat recovery from geothermal source of heat
WO2007098370A2 (en) 2006-02-16 2007-08-30 Chevron U.S.A. Inc. Kerogen extraction from subterranean oil shale resources
RU2008145876A (en) 2006-04-21 2010-05-27 Шелл Интернэшнл Рисерч Маатсхаппий Б.В. (NL) HEATERS WITH RESTRICTION OF TEMPERATURE WHICH USE PHASE TRANSFORMATION OF FERROMAGNETIC MATERIAL
CA2667274A1 (en) 2006-10-20 2008-05-02 Shell Internationale Research Maatschappij B.V. Systems and processes for use in treating subsurface formations
US20080216323A1 (en) 2007-03-09 2008-09-11 Eveready Battery Company, Inc. Shaving preparation delivery system for wet shaving system
EP2142758A1 (en) 2007-04-20 2010-01-13 Shell Internationale Research Maatschappij B.V. Parallel heater system for subsurface formations
US7866386B2 (en) 2007-10-19 2011-01-11 Shell Oil Company In situ oxidation of subsurface formations
EP2262978A1 (en) 2008-04-18 2010-12-22 Shell Internationale Research Maatschappij B.V. Using mines and tunnels for treating subsurface hydrocarbon containing formations

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN85109007A (en) * 1985-12-09 1987-06-24 国际壳牌研究有限公司 Method and apparatus for installation of electric heater
CN1236858A (en) * 1998-03-06 1999-12-01 国际壳牌研究有限公司 Electrical heater
CN1430696A (en) * 2000-04-24 2003-07-16 国际壳牌研究有限公司 Heating system and method
CN1430695A (en) * 2000-04-24 2003-07-16 国际壳牌研究有限公司 Electrical well heating system and method

Also Published As

Publication number Publication date
AU2011201030A8 (en) 2011-04-21
EP1871980A1 (en) 2008-01-02
CA2605720A1 (en) 2006-11-02
AU2006239996A1 (en) 2006-11-02
AU2011201030B2 (en) 2013-02-14
MA29472B1 (en) 2008-05-02
EA200702297A1 (en) 2008-04-28
ZA200708021B (en) 2008-10-29
DE602006006042D1 (en) 2009-05-14
ATE435964T1 (en) 2009-07-15
AU2006239997B2 (en) 2010-06-17
DE602006007693D1 (en) 2009-08-20
CA2605729C (en) 2015-07-07
CA2606217A1 (en) 2006-11-02
IL186209A0 (en) 2008-01-20
EA200702300A1 (en) 2008-04-28
AU2006239961A1 (en) 2006-11-02
IL186209A (en) 2013-03-24
WO2006116096A1 (en) 2006-11-02
NZ562244A (en) 2010-12-24
NZ562249A (en) 2010-11-26
US20070108201A1 (en) 2007-05-17
WO2006116095A1 (en) 2006-11-02
CA2605729A1 (en) 2006-11-02
CA2606165C (en) 2014-07-29
CN101163855A (en) 2008-04-16
EA012900B1 (en) 2010-02-26
CA2606217C (en) 2014-12-16
CA2606295A1 (en) 2006-11-02
EA200702303A1 (en) 2008-04-28
CN101163853A (en) 2008-04-16
MA29471B1 (en) 2008-05-02
WO2006115945A1 (en) 2006-11-02
NZ562250A (en) 2010-12-24
MA29474B1 (en) 2008-05-02
WO2006116097A1 (en) 2006-11-02
CA2606216A1 (en) 2006-11-02
WO2006116133A1 (en) 2006-11-02
CN101163780A (en) 2008-04-16
EA014760B1 (en) 2011-02-28
AU2006239962B8 (en) 2010-04-29
WO2006116078A1 (en) 2006-11-02
CN101163857B (en) 2012-11-28
ZA200708087B (en) 2008-10-29
CA2606216C (en) 2014-01-21
ZA200708088B (en) 2008-10-29
AU2006239999B2 (en) 2010-06-17
CA2605724A1 (en) 2006-11-02
AU2006240175B2 (en) 2011-06-02
AU2006239996B2 (en) 2010-05-27
EA200702304A1 (en) 2008-02-28
EP1871978B1 (en) 2016-11-23
IN266867B (en) 2015-06-10
CA2605737A1 (en) 2006-11-02
NZ562240A (en) 2010-10-29
EA200702305A1 (en) 2008-02-28
NZ562248A (en) 2011-01-28
CN101163860B (en) 2013-01-16
EA012767B1 (en) 2009-12-30
CA2606218A1 (en) 2006-11-02
CN101163856A (en) 2008-04-16
CA2605724C (en) 2014-02-18
EP1871981A1 (en) 2008-01-02
NZ562241A (en) 2010-12-24
AU2006239963A1 (en) 2006-11-02
MA29469B1 (en) 2008-05-02
CA2606176A1 (en) 2006-11-02
CA2606210A1 (en) 2006-11-02
CA2606210C (en) 2015-06-30
CN101163852B (en) 2012-04-04
AU2006239961B2 (en) 2010-03-18
CN101163854A (en) 2008-04-16
EP1871979A1 (en) 2008-01-02
IL186207A0 (en) 2008-01-20
IL186211A (en) 2011-12-29
AU2006240173B2 (en) 2010-08-26
WO2006116087A1 (en) 2006-11-02
NZ562243A (en) 2010-12-24
MA29475B1 (en) 2008-05-02
EA012554B1 (en) 2009-10-30
EP1871987A1 (en) 2008-01-02
IL186205A (en) 2012-06-28
EP1871986A1 (en) 2008-01-02
IL186204A (en) 2012-06-28
AU2006239962A1 (en) 2006-11-02
CN101300401A (en) 2008-11-05
ATE434713T1 (en) 2009-07-15
CA2605737C (en) 2015-02-10
AU2006239963B2 (en) 2010-07-01
AU2006240173A1 (en) 2006-11-02
IL186203A0 (en) 2008-01-20
CA2606181A1 (en) 2006-11-02
AU2006240043A1 (en) 2006-11-02
CN101163857A (en) 2008-04-16
IL186213A0 (en) 2008-06-05
CN101163851A (en) 2008-04-16
EP1871985A1 (en) 2008-01-02
EP1871985B1 (en) 2009-07-08
ZA200708136B (en) 2008-09-25
CA2606295C (en) 2014-08-26
WO2006116130A1 (en) 2006-11-02
CN101163859B (en) 2012-10-10
ATE437290T1 (en) 2009-08-15
AU2006240033A1 (en) 2006-11-02
AU2006239958A1 (en) 2006-11-02
AU2006240033B2 (en) 2010-08-12
EA012171B1 (en) 2009-08-28
EP1871978A1 (en) 2008-01-02
US7831133B2 (en) 2010-11-09
EA200702296A1 (en) 2008-04-28
EA014031B1 (en) 2010-08-30
IL186210A (en) 2011-10-31
MA29473B1 (en) 2008-05-02
MA29719B1 (en) 2008-09-01
ZA200708135B (en) 2008-10-29
IL186212A0 (en) 2008-01-20
IL186214A0 (en) 2008-01-20
AU2006239886A1 (en) 2006-11-02
EA200702302A1 (en) 2008-04-28
CA2606181C (en) 2014-10-28
EP1871982B1 (en) 2010-04-07
CN101163858A (en) 2008-04-16
CN101163860A (en) 2008-04-16
MA29470B1 (en) 2008-05-02
EP1871990B1 (en) 2009-06-24
CN101163859A (en) 2008-04-16
EA011905B1 (en) 2009-06-30
EP1871987B1 (en) 2009-04-01
IL186204A0 (en) 2008-01-20
DE602006007974D1 (en) 2009-09-03
WO2006116207A3 (en) 2007-06-14
ZA200708022B (en) 2008-10-29
MA29468B1 (en) 2008-05-02
EA200702306A1 (en) 2008-02-28
ZA200708020B (en) 2008-09-25
ZA200708023B (en) 2008-05-28
CA2605720C (en) 2014-03-11
IL186213A (en) 2011-08-31
CN101163852A (en) 2008-04-16
EP1871982A1 (en) 2008-01-02
CA2606165A1 (en) 2006-11-02
IL186214A (en) 2011-12-29
NZ562242A (en) 2010-12-24
ATE463658T1 (en) 2010-04-15
WO2006116092A1 (en) 2006-11-02
MA29478B1 (en) 2008-05-02
DE602006007450D1 (en) 2009-08-06
NZ562247A (en) 2010-10-29
IL186210A0 (en) 2008-01-20
EA012077B1 (en) 2009-08-28
EP1871858A2 (en) 2008-01-02
EA200702299A1 (en) 2008-04-28
IL186206A (en) 2011-12-29
EA200702307A1 (en) 2008-02-28
CN101163856B (en) 2012-06-20
NZ562252A (en) 2011-03-31
NZ562251A (en) 2011-09-30
EA014258B1 (en) 2010-10-29
EP1871983B1 (en) 2009-07-22
EA013555B1 (en) 2010-06-30
EA011226B1 (en) 2009-02-27
WO2006116131A1 (en) 2006-11-02
AU2006239999A1 (en) 2006-11-02
EP1871983A1 (en) 2008-01-02
IL186203A (en) 2011-12-29
ZA200708316B (en) 2009-05-27
EA012901B1 (en) 2010-02-26
ZA200708137B (en) 2008-10-29
CN101163780B (en) 2015-01-07
ZA200708089B (en) 2008-10-29
AU2011201030A1 (en) 2011-03-31
DE602006013437D1 (en) 2010-05-20
IL186212A (en) 2014-08-31
CN101163855B (en) 2011-09-28
CA2606176C (en) 2014-12-09
CN101163854B (en) 2012-06-20
AU2006239958B2 (en) 2010-06-03
AU2006239962B2 (en) 2010-04-01
ATE427410T1 (en) 2009-04-15
AU2006239997A1 (en) 2006-11-02
IL186207A (en) 2011-12-29
MA29476B1 (en) 2008-05-02
IL186206A0 (en) 2008-01-20
EA200702301A1 (en) 2008-04-28
IL186211A0 (en) 2008-01-20
AU2006239886B2 (en) 2010-06-03
NZ562239A (en) 2011-01-28
ZA200708134B (en) 2008-10-29
CA2606218C (en) 2014-04-15
EA200702298A1 (en) 2008-04-28
MA29477B1 (en) 2008-05-02
EP1871990A1 (en) 2008-01-02
WO2006116207A2 (en) 2006-11-02
CN101300401B (en) 2012-01-11
AU2006240043B2 (en) 2010-08-12
AU2006240175A1 (en) 2006-11-02
ZA200708090B (en) 2008-10-29
WO2006115943A1 (en) 2006-11-02
IL186205A0 (en) 2008-01-20
CN101163858B (en) 2012-02-22
EP1880078A1 (en) 2008-01-23
IL186208A (en) 2011-11-30
IL186208A0 (en) 2008-01-20

Similar Documents

Publication Publication Date Title
CN101163853B (en) Insulation conductor temperature-limiting heater for underground strata heating combined with three-phase y structure
CN1957158B (en) Temperature limited heaters used to heat subsurface formations
ZA200608263B (en) Temperature limited heaters with thermally conductive fluid used to heat subsurface formations

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20120321

Termination date: 20170421

CF01 Termination of patent right due to non-payment of annual fee